Synthesis of Polymer-Based Magnetic Nanocomposite for Multi-Pollutants Removal from Water

A magnetic polymer-based nanocomposite was fabricated by the modification of an Fe3O4/SiO2 magnetic composite with polypyrrole (PPy) via co-precipitation polymerization to form PPy/Fe3O4/SiO2 for the removal of Congo red dye (CR) and hexavalent chromium Cr(VI) ions from water. The nanocomposite was characterized using various techniques including X-ray diffraction (XRD), Fourier transform infrared spectroscopy (FTIR), scanning electron microscope (SEM), vibration sample magnetometer, and thermogravimetric analysis (TGA). The results confirm the successful fabrication of the nanocomposite in the size of nanometers. The effect of different conditions such as the contact time, adsorbent dosage, solution pH, and initial concentration on the adsorption process was investigated. The adsorption isotherm suggested monolayer adsorption of both contaminants over the PPy/Fe3O4/SiO2 nanocomposite following a Langmuir isotherm, with maximum adsorption of 361 and 298 mg.g−1 for CR dye and Cr(VI), respectively. Furthermore, the effect of water type on the adsorption process was examined, indicating the applicability of the PPy/Fe3O4/SiO2 nanocomposite for real sample treatment. Interestingly, the reusability of the nanocomposite for the removal of the studied contaminants was investigated with good results even after six successive cycles. All results make this nanocomposite a promising material for water treatment.


Introduction
Industrial wastewater treatment has become increasingly complex in recent decades as a result of the rapid industrialization and the presence of complex mixtures of toxic metal ions and organic dyes that harm human health and the environment [1][2][3]. The textile, paper, and plastic industries are the most common manufacturing purposes including dyes as important aromatic compounds [4]. In addition to their carcinogenic effects, contaminated drinking water with dyes causes various symptoms including severe headaches, skin irritation, and acute diarrhea [5]. Similarly, metal ions are not less dangerous than organic dyes due to their high toxicity when discharged in water supplies [6]. One of these toxic metals, hexavalent chromium (Cr(VI)), is classified as a very toxic and carcinogenic metal, causing nephritis, gastrointestinal ulceration, and cancer in the digestive tract [7]. The accepted concentrations of hexavalent chromium in drinking water and industrial

Synthesis of Fe 3 O 4 /SiO 2 /PPy Magnetic Nanocomposite
The synthesis of the Fe 3 O 4 /SiO 2 /PPy magnetic nanocomposite was achieved in three steps. The first step included the synthesis of Fe 3 O 4 nanoparticles, which was followed by the second step consisting of the modification of Fe 3 O 4 nanoparticles with SiO 2 . The third step included the formation of polypyrrole over the Fe 3 O 4 /SiO 2 composite. For Fe 3 O 4 nanoparticle synthesis, we followed the literature [29] in which hydrochloric acid (HCl, 0.5 M, 100 mL) was used for dissolving ammonia iron sulfate ((NH 4 ) 2 Fe(SO 4 ) 2 ·6H 2 O), 7.85g) and ferric chloride (FeCl 3 , 10.82 g), followed by placing this mixture at 30 • C in an ultrasound bath for half an hour. After that, the temperature of the mixture was adjusted at 80 • C, aqueous ammonia (25%, 60 mL) was added drop-wise, and the solution was stirred at 1500 rpm to form the Fe 3 O 4 nanoparticles as a black precipitate. The stirring process of the mixture was continued up to one hour followed by collecting the nanoparticles via an external magnet, and the collected Fe 3 O 4 nanoparticles were washed several times with distilled water and dried for half a day at 70 • C in an oven. Finally, Fe 3 O 4 nanoparticles were ready to be used. In the second step, Fe 3 O 4 nanoparticles were modified with SiO 2 by using tetraethyl orthosilicate (TEOS). This was achieved by using a mixture of distilled H 2 O (40 mL) and ethyl alcohol (99.9%, 170 mL) to dissolve 2.0 g of synthesized Fe 3 O 4 nanoparticles. Then, after adding 6 mL of aqueous ammonia, this mixture was placed for 15.0 min at 30 • C in an ultrasound bath. After the complete dispersion of Fe 3 O 4 with vigorous stirring up to half a day under argon gas environment, 2 mL of TEOS was added to the solution. The synthesized Fe 3 O 4 /SiO 2 was then collected by an external magnet, washed several times with absolute ethyl alcohol, and finally dried at 70 • C in an oven for four hours. The final step was the formation of PPy over the synthesized Fe 3 O 4 /SiO 2 composite via the co-precipitation chemical method. In a glass beaker, 100 mL of distilled water was used to disperse 1.0 g of Fe 3 O 4 /SiO 2 nanoparticles. For the complete dispersion of nanoparticles, the beaker was placed for 15.0 min at 30 • C in an ultrasound bath. After that, the solution was stirred vigorously and during that, pyrrole (0.1 M) was added and the stirring was continued up to two hours followed by the addition of ferric chloride (0.1 M, 50.0 mL); the reaction was continued for an additional three hours. Finally, the synthesized nanocomposite of PPy/Fe 3 O 4 /SiO 2 was collected by an external magnet, washed several times with absolute ethyl alcohol, and then dried in an oven at 60.0 • C for 6.0 h.

Material Characterization
The synthesized materials were characterized using various techniques including X-ray diffraction (XRD), magnetometer, Fourier transform infrared spectroscopy (FT-IR), scanning electron microscope (SEM), and thermogravimetric analysis (TGA) measurement. A GNR APD-2000 PRO (GNR, Cairo, Egypt) diffractometer was used to measure XRD using Cu Ka radiation (λ = 1.5406 Å), operating at 45 kV. The diffraction intensities were recorded over 2θ ranging from 5 • to 60 • with a 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. A Bruker, Tensor 27 FT-IR (BRUKER, Karlsruhe, Germany) spectrophotometer was used to perform FT-IR spectra in the range of 400-4000 cm −1 at room temperature and collected these at a resolution of 4 cm −1 . An SEM Hitachi S4800 (Hitachi, Tokyo, Japan) was used to study the morphology of the synthesized material. A Perkin Elmer STA 6000 (PerkinElmer Inc., Shelton, USA) was used to measure the thermogravimetric analysis for the evaluation of thermal stability. The effect of the contact time on the removal of Cr(VI) and Congo red from water using the PPy/Fe 3 O 4 /SiO 2 nanocomposite was studied using a volume of 100 mL of contaminated water (100 mg.L −1 ) and adsorbent mass of 0.02 g at pH of 4.0. The solution shaking was conducted up to 24 h with sampling at various times to investigate the remaining contaminants using ICP and a UV-Vis spectrophotometer. The adsorbent was collected after each experiment using a magnet. All experiments were performed in triplicate.

The Effect of Adsorbent Dosage
Different masses of the adsorbent PPy/Fe 3 O 4 /SiO 2 nanocomposite were used to study the effect of adsorbent dosage on the removal of Cr(VI) and Congo red. The definite mass of adsorbent was mixed with 100.0 mL of polluted water with pH of 4.0 up to 12 h. When equilibrium was reached, the adsorbent was collected with a magnet, and the solution was examined for the presence of Cr(VI) and Congo red. Experiments were performed in triplicate.

The Effect of Solution pH
A pH range of 3.0 to 7.0 was used to investigate the pH effect on the removal of Cr(VI) and Congo red using the PPy/Fe 3 O 4 /SiO 2 nanocomposite. The adsorbent mass used was 0.05 g, the time was 12.0 h, and the solution volume was 100.0 mL. After each experiment, magnetic separation was used to collect the adsorbent, and the solution was examined for any residual pollutants using ICP and a UV-Vis spectrophotometer (Hach, CO, USA). Experiments were performed in triplicate.

The Adsorption Isotherm
To study the maximum adsorption capacity and the type of the adsorption process of Cr(VI) and Congo red over the synthesized PPy/Fe 3 O 4 /SiO 2 nanocomposite, the contaminated solution (100.0 mL) was mixed with 0.02 g of the composite for 24.0 h at pH 4.0. The adsorption mechanism was represented by three isotherm models: Freundlich, Langmuir, and Temkin.

The Regeneration Study
To assess the commercial application of an adsorbent, it is necessary to determine the reusability of the material for the effective removal of contaminants several times. This was achieved by performing the adsorption experiment 6.0 successive times by mixing the contaminated water (100 mg.L −1 , 100 mL, pH 4.0) with adsorbent (0.05 g) for 12.0 h. After each cycle, the adsorbent was collected with an external magnet, washed with distilled water extensively, and then dried at 50.0 • C for 5.0 h to be used in the next cycle. Experiments were performed in triplicate.

Water Type Effect
Different types of water including wastewater, groundwater, tap water, and distilled water were used to determine the water type effect on the removal of Cr(VI) and Congo red using the synthesized PPy/Fe 3 O 4 /SiO 2 nanocomposite. Polluted solution prepared using target water with a concentration of 100.0 mg.L −1 and volume of 100.0 mL was mixed with 0.05 g of adsorbent for 12 h. After each experiment, the solution was examined for the presence of contaminants.

Nanocomposite Characterization
The synthesized materials including Fe 3 O 4 , Fe 3 O 4 /SiO 2 , and PPy/Fe 3 O 4 /SiO 2 nanomaterials were investigated using different techniques such as X-ray diffraction (XRD),  Figure 1a. The XRD of Fe 3 O 4 nanoparticles alone indicated the cubic phase structure, and the peaks correspond to the (511), (422), (400), (311), and (220) crystalline planes [30]. The XRD of the Fe 3 O 4 /SiO 2 composite showed the appearance of all Fe 3 O 4 peaks with the reduction in the peak intensity and the disappearance of the peak at 2θ = 20 [31] indicating the crystallinity decrease in Fe 3 O 4 by the combination with amorphous SiO 2 . The XRD of the PPy/Fe 3 O 4 /SiO 2 nanocomposite showed the appearance of all Fe 3 O 4 peaks, and there was an overlap between the two peaks of Fe 3 O 4 and PPy at 2θ = 20 that made this peak wider [32]. The diffraction intensity of this peak showed a clearly increase linked to the marked increase in the thickness of the polypyrrole shell, indicating the existence of amorphous polypyrrole in the sample. Additionally, the amorphous structure of SiO 2 and PPy caused a reduction in the intensity of  [35]. Additionally, the NOH peak appeared at 934 cm −1 and the C-N peak appeared at 1192 cm −1 . Additionally, the C-H vibrations were represented by the peaks at 1052, 1300, and 1298 cm −1 [36]. The pyrrole ring vibrations were represented by the peaks at 1552 and 1547 cm −1 . The wide peak observed at the range of 3500-3000 is characteristic of PPy composites, due to the N-H bonds' large number [28]. Furthermore, the N-H and O-H vibrations were represented by the peaks at 3447 and 3434 cm −1 [28,36]. The results of FT-IR are in excellent agreement with previous studies of Fe 3 O 4 , Fe 3 O 4 /SiO 2 [29], and PPy and its compounds [37].
An advantage of the present nanocomposite is its magnetic properties that allow its separation from the experimental media. Therefore, the magnetization curves of the synthesized materials Fe 3 O 4 , Fe 3 O 4 /SiO 2 , and PPy/Fe 3 O 4 /SiO 2 at room temperature are shown in Figure 1c. According to Figure 1c, the highest saturation magnetization was observed at 68 emu.g −1 for Fe 3 O 4 nanoparticles. This value dropped to 35 emu.g −1 after the modification of Fe 3 O 4 with silica, indicating the effective interaction between Fe 3 O 4 and SiO 2 [38]. Moreover, the successful modification of the composite Fe 3 O 4 /SiO 2 with PPy was indicated by the dropped value of saturation magnetization to 8 emu.g −1 , indicating that the SiO 2 layer was thinner than the PPy layer [39]. It can be noticed that all synthesized materials have good magnetic properties, allowing magnetic separation using an external magnet, as shown in (Figure 1c, inset).
The thermal stability of the synthesized nanomaterials (Fe 3 O 4 , Fe 3 O 4 /SiO 2 , and PPy/Fe 3 O 4 /SiO 2 ) was investigated using thermogravimetric analysis (TGA), as shown in Figure 1d. According to the TGA curve of Fe 3 O 4 , there is a minor weight loss (in the temperature range of room temperature to 10,000 • C) equal to about 3.0% that is attributed to the evaporation of the chemical or physical attached water or hydroxyl groups on the surface of Fe 3 O 4 nanoparticles. The TGA curve of Fe 3 O 4 /SiO 2 indicated the successful deposition of thermally stable SiO 2 on the Fe 3 O 4 surface as there was only 3.5% weight loss in the temperature from room temperature to 161 • C, which is attributed to the evaporation of adsorbed water. The TGA curve of the PPy/Fe 3 O 4 /SiO 2 nanocomposite showed 5.0% weight loss at the temperature range from room temperature to 300.0 • C, which is attributed to the removal of the PPy monomer and the evaporation of adsorbed water. Ppy chains  The thermal stability of the synthesized nanomaterials (Fe3O4, Fe3O4/SiO2, and PPy/Fe3O4/SiO2) was investigated using thermogravimetric analysis (TGA), as shown in Figure 1d. According to the TGA curve of Fe3O4, there is a minor weight loss (in the temperature range of room temperature to 10,000 °C) equal to about 3.0% that is attributed to the evaporation of the chemical or physical attached water or hydroxyl groups on the surface of Fe3O4 nanoparticles. The TGA curve of Fe3O4/SiO2 indicated the successful deposition of thermally stable SiO2 on the Fe3O4 surface as there was only 3.5% weight loss in the temperature from room temperature to 161 °C, which is attributed to the evaporation of adsorbed water. The TGA curve of the PPy/Fe3O4/SiO2 nanocomposite showed 5.0% weight loss at the temperature range from room temperature to 300.0 °C, which is attributed to the removal of the PPy monomer and the evaporation of adsorbed water. Ppy chains have good thermal stability and can be destroyed at high temperatures only. This fact is indicated by the sharp peak at 640.0 °C and weak peak at 400.0 to 500.0 °C. The low  [29], and PPy composites [40] from the view of particle shape, morphology, and porosity. The SEM image of Fe3O4 nanoparticles indicated their granular shape with a size range of 40.0 to 100.0 nm (in Figure 1a). Similar granular shapes with no big differences in porosity, morphology, and structure were observed between the Fe3O4/SiO2 composite ( Figure 2b) and Fe3O4 nanoparticles. However, the morphology of the particles was changed by the addition of PPy, as shown in Figure 2c. The particles became cabbage in shape with an increase in their size as expected due to the deposition of pyrrole over Fe3O4 firstly, followed by the synthesis of PPy, causing the size increase. The present results are in agreement with the previous studies of Fe3O4 nanoparticles, Fe3O4/SiO2 composites [29], and PPy composites [40] from the view of particle shape, morphology, and porosity.

Effect of Contact Time
The effect of the contact time on the removal of Cr(VI) and Congo red dye from water using the magnetic PPy/Fe3O4/SiO2 nanocomposite was studied, as shown in Figure 3a. According to Figure 3a, there were two stages of removal of both pollutants. The first stage showed a rapid removal of Cr(VI) and Congo red dye that appeared in the plot as a linear

Effect of Contact Time
The effect of the contact time on the removal of Cr(VI) and Congo red dye from water using the magnetic PPy/Fe 3 O 4 /SiO 2 nanocomposite was studied, as shown in Figure 3a. According to Figure 3a, there were two stages of removal of both pollutants. The first stage showed a rapid removal of Cr(VI) and Congo red dye that appeared in the plot as a linear curve. The second stage showed stable removal of Cr(VI) and Congo red dye, which appeared in the plot as a plateau curve, meaning that the adsorption process reached equilibrium.
This behavior can be explained in that the first stage occurred due to the existence of a large number of empty adsorption sites on the adsorbent surface, allowing the rapid capture of pollutants within a short period. After that, the adsorption sites became filled, and equilibrium was achieved [41,42]. According to Figure 3a capture of pollutants within a short period. After that, the adsorption sites became filled, and equilibrium was achieved [41,42]. According to Figure 3a, the Cr(VI) and Congo red dye removal by the magnetic PPy/Fe3O4/SiO2 nanocomposite increased from 8.0 to 193.0 mg.g −1 and from 17.0 to 213.0 mg.g −1 , respectively, when the contact time increased from 5.0 to 1440.0 min. As clearly shown in the contact time plot, 480.0 min was the point at which equilibrium was reached for the removal of Cr(VI) and Congo red dye using the PPy/Fe3O4/SiO2 nanocomposite.   Figure 3b shows the effect of adsorbent dosages on the removal of Cr(VI) and Congo red dye from water using the PPy/Fe 3 O 4 /SiO 2 nanocomposite. This was achieved using different masses of the nanocomposite as follows: 0.06, 0.05, 0.04, 0.03, 0.02, and 0.01 g. According to Figure 3b, the increased dose of the nanocomposite led to an increase in the removal percentage of both pollutants. This behavior is attributed to the existence of accessible and sufficient adsorption sites for the uptake of Cr(VI) and Congo red, which are increased by adding more quantities of the adsorbent, as reported in previous studies [43]. According to the Figure 3b, the removal efficiencies of Cr(VI) and Congo red were increased from 16.0% to 98.0% and from 19.0% to 99.5%, respectively, when the mass of the PPy/Fe 3 O 4 /SiO 2 nanocomposite increased from 0.01 to 0.06 g. When the adsorbent mass increased from 0.05 to 0.06 g, there was no significant increase in the removal efficiencies. Therefore, 0.05 g was considered the optimum adsorbent dose for the removal of both contaminants using the PPy/Fe 3 O 4 /SiO 2 nanocomposite. This behavior may be attributed to the saturation of the adsorption sites or the agglomeration of adsorbent particles when their quantity increased, leading to the constant removal efficiency [44].

Effect of Solution pH
The pH effect on the removal of Cr(VI) and Congo red using the PPy/Fe 3 O 4 /SiO 2 nanocomposite was investigated in the range of 3.0 to 8.0, as shown in Figure 3c. According to Figure 3c, the highest removal efficiencies were achieved at the lowest pH (3.0 to 4.0) with removal values of 99.0% and 99.7% for Cr(VI) and Congo red, respectively. Moreover, the pH increase allowed a removal efficiency decrease for both Cr(VI) and Congo red. This behavior is attributed to many factors such as the charge in adsorbates and the adsorbent surface charge in the water environment. The increased removal efficiency at very low pH values is attributed to the high electrostatic attractions between the negatively charged adsorbates (acidic CR dye and Cr(VI)) and the protonated adsorbent functional groups. The decreased removal efficiency at a higher pH value is attributed to the existence of negatively charged hydroxyl groups that compete with adsorbate molecules for adsorption active sites. Additionally, Cr 2 O 7 2− and HCrO 4 − are the predominant ions of chromium in the pH range of (2.0 to 6.0), while this form changes by a pH increase to HCrO 4 2− . It is well known that the HCrO 4 − form of chromium ions has the lowest adsorption energy equal to (0.60 to 2.50 kcal.mol −1 ) [45] that explains their high removal at a lower pH. Moreover, at a low pH, H + ions neutralize the negatively charged adsorbent surface, thereby reducing the barrier to diffusion of dichromate ions. However, the pH effect may be controlled by the development of an electric double layer over the adsorbent. With the increase in pH, the concentration of H + ions changes from acidic to basic, and, consequently, the polarity of the double layer at the adsorbent surface may be changed from positive to negative. At a lower pH, the system attained equilibrium faster and also the percentage of chromium adsorbed increased, as explained by Verma et al. [46]. Finally, we can conclude that the adsorption behavior at different pH values is dependent on the protonation or deprotonation of the adsorbent functional groups which detect the attraction or repulsion forces between these functional groups and metallic ions and dyes. Therefore, the adsorbent active binding sites and surface chemistry of the material are clearly influenced by the pH, which affects the efficiency of the adsorption. Figure 3d shows the effect of using different Congo red dye and Cr(VI) initial concentrations on their adsorption over the PPy/Fe 3 O 4 /SiO 2 nanocomposite. This was achieved by using a concentration range of 25.0-300.0 mg.L −1 for both Congo red dye and Cr(VI). According to Figure 3d, the adsorption capacity increased by increasing the initial concentration of Congo red dye and Cr(VI), and at a certain point, equilibrium was reached (the adsorption increase became slower). Equilibrium was reached at 100.0 mg.L −1 for both Congo red dye and Cr(VI), which is considered the optimum initial concentration. The maximum adsorption capacities reached 207.0 mg.L −1 and 257.0 mg.L −1 for Cr(VI) and Congo red dye, respectively. These highest values of pollutant removal at higher concentrations could be explained on the basis of the high attraction forces between pollutants and the adsorbent surface at high concentrations.

Adsorption Isotherm
Freundlich, Langmuir, and Temkin adsorption isotherms were used to investigate the adsorption isotherm of Congo red dye and Cr(VI) ions over the surface of the PPy/Fe 3 O 4 /SiO 2 nanocomposite. The main purpose of studying the adsorption isotherm is to understand the adsorption mechanism over the studied adsorbent (i.e., assess the adsorption limit and the distribution of the pollutants on the adsorbent sites). The fitting of isotherms is presented in Figure 4. adsorption of contaminants over the surface of the adsorbent, and the adsorption was achieved via the construction of a monolayer from the pollutant ions [48]. The Langmuir model can be represented by the equation where KL denotes the Langmuir constant and qm denotes maximum adsorption after reaching saturation.
where B and A denote Temkin model constants. Table 1 summarizes the Freundlich and Langmuir parameters for the removal of Congo red dye and Cr(VI) ions over the PPy/Fe3O4/SiO2 nanocomposite. According to the data in Table 1, there was a lower fit of the Freundlich and Temkin isotherms than the Langmuir isotherm for the adsorption of Congo red dye and Cr(VI) The first studied isotherm was the Freundlich model that suggested heterogeneous adsorption of contaminants over the surface of the adsorbent, and the adsorption was achieved via the construction of multilayers from the pollutant ions [47]. The Freundlich model can be represented by the equation where q e denotes the amount of uptake pollutants after equilibration (mg.g −1 ), C e denotes the rest concentrations (mg.L −1 ), and N and K F are the normal constants of the Freundlich model and related to the adsorption intensities and capacities, respectively. The second studied isotherm was the Langmuir model that suggested homogenous adsorption of contaminants over the surface of the adsorbent, and the adsorption was achieved via the construction of a monolayer from the pollutant ions [48]. The Langmuir model can be represented by the equation q e = K L q m /(1 + K L C e ), (2) where K L denotes the Langmuir constant and q m denotes maximum adsorption after reaching saturation. The last model is the Temkin isotherm that indicates the effect of sorbate ions on each other during the adsorption process. The Temkin model can be represented by the equation where B and A denote Temkin model constants.  According to the data in Table 1, there was a lower fit of the Freundlich and Temkin isotherms than the Langmuir isotherm for the adsorption of Congo red dye and Cr(VI) metal on the surface of the PPy/Fe 3 O 4 /SiO 2 nanocomposite, as indicated from the values of R 2 . The maximum adsorption capacities of the PPy/Fe 3 O 4 /SiO 2 nanocomposite calculated using the Langmuir model were found to be 298.22 mg.g −1 and 361.43 mg.g −1 for Cr(VI) and Congo red dye, respectively. Subsequently, the adsorption of Cr(VI) and Congo red dye on the surface of the PPy/Fe 3 O 4 /SiO 2 nanocomposite was achieved in the form of monolayer uptake on the energetically symmetrical (homogeneous) adsorption sites. Additionally, the values of N obtained from fitting of the experimental data with the Freundlich isotherm were higher than zero, indicating the favorable adsorption of both pollutants. Additionally, the experimental data also fitted the Temkin model, indicating that the adsorption process was possibly affected by pollutant ion interactions.

The Regeneration Study
The application of any studied adsorbent at a large scale for wastewater treatment essentially requires an investigation of its regeneration [49,50]. Concerning this, the reusability of the PPy/Fe 3 O 4 /SiO 2 nanocomposite for the removal of Cr(VI) ions and Congo red dye was studied for up to six successive cycles, as shown in Figure 5a.
After each cycle, the adsorbent was separated using an external magnet, washed several times extensively with distilled water to remove any adhered pollutants, and then dried in an oven to be used in the next adsorption-desorption cycle. The studied PPy/Fe 3 O 4 /SiO 2 nanocomposite showed good reusability for the removal of Cr(VI) and Congo red dye during the studied cycles, with a decrease in the efficiencies by increasing the cycles. The composite's efficiency to remove Congo red dropped from 98.0% to 74.0%, while for Cr(VI) removal, it dropped from 93.0% to 72.0% after six reuse cycles. This behavior is attributed to the destroyed adsorption sites over the nanocomposite surface after each cycle, causing the decrease in the material efficiency to capture the pollutants.

The Regeneration Study
The application of any studied adsorbent at a large scale for wastewater treatment essentially requires an investigation of its regeneration [49,50]. Concerning this, the reusability of the PPy/Fe3O4/SiO2 nanocomposite for the removal of Cr(VI) ions and Congo red dye was studied for up to six successive cycles, as shown in Figure 5a. After each cycle, the adsorbent was separated using an external magnet, washed several times extensively with distilled water to remove any adhered pollutants, and then dried in an oven to be used in the next adsorption-desorption cycle. The studied PPy/Fe3O4/SiO2 nanocomposite showed good reusability for the removal of Cr(VI) and Congo red dye during the studied cycles, with a decrease in the efficiencies by increasing the cycles. The composite's efficiency to remove Congo red dropped from 98.0% to 74.0%, while for Cr(VI) removal, it dropped from 93.0% to 72.0% after six reuse cycles. This behavior is attributed to the destroyed adsorption sites over the nanocomposite surface after each cycle, causing the decrease in the material efficiency to capture the pollutants.

The Water Type Effect
The removal efficiency of Cr(VI) ions and Congo red dye on the surface of the PPy/Fe3O4/SiO2 nanocomposite using different types of water including sewage water, groundwater, tap water, and distilled water was investigated to determine the applicability of the synthesized nanocomposite for an effective real water treatment (Figure 5b). The order of the removal efficiency for both pollutants (Cr(VI) and Congo red dye) was distilled water > tap water > groundwater > sewage water. This resulting behavior is attributed to the existence of other contaminants in each water type that compete with the studied pollutants for the adsorption active sites over the nanocomposite surface. Furthermore, the selectivity of any innovative adsorbent should be studied toward different competing co-ions including bicarbonate, sulfate, and chloride ions that may be present in water. For example, it was reported that sulphate and chloride negatively affect the adsorption of Cr(VI) on polypyrrole@magnetic chitosan nanocomposites [51]. Additionally, the similarity of the ionic charge between Cr(VI) and bicarbonate ions showed a competitive effect on the adsorption of Cr(VI) [51,52]. Therefore, it is very important to determine the chemical composition of the water before starting the adsorption experiments. Matched to the reported concentrations in nature, these removal efficiencies were

The Water Type Effect
The removal efficiency of Cr(VI) ions and Congo red dye on the surface of the PPy/Fe 3 O 4 /SiO 2 nanocomposite using different types of water including sewage water, groundwater, tap water, and distilled water was investigated to determine the applicability of the synthesized nanocomposite for an effective real water treatment (Figure 5b). The order of the removal efficiency for both pollutants (Cr(VI) and Congo red dye) was distilled water > tap water > groundwater > sewage water. This resulting behavior is attributed to the existence of other contaminants in each water type that compete with the studied pollutants for the adsorption active sites over the nanocomposite surface. Furthermore, the selectivity of any innovative adsorbent should be studied toward different competing co-ions including bicarbonate, sulfate, and chloride ions that may be present in water. For example, it was reported that sulphate and chloride negatively affect the adsorption of Cr(VI) on polypyrrole@magnetic chitosan nanocomposites [51]. Additionally, the similarity of the ionic charge between Cr(VI) and bicarbonate ions showed a competitive effect on the adsorption of Cr(VI) [51,52]. Therefore, it is very important to determine the chemical composition of the water before starting the adsorption experiments. Matched to the reported concentrations in nature, these removal efficiencies were achieved for a pollutant concentration of 100.0 mg.L −1 , which is considered high. This fact approves the applicability of the PPy/Fe 3 O 4 /SiO 2 nanocomposite for real water treatment.

Comparative Study
The assessment of the synthesized nanocomposite for the removal of Congo red dye and Cr(VI) ions required its comparison with previously reported adsorbents. In this regard, we summarized the previously studied adsorbents for the removal of Congo red dye and Cr(VI) ions in Table 2. According to Table 2 [53][54][55][56][57][58][59][60][61][62][63][64][65][66][67][68], it is noticeable that the present synthesized PPy/Fe 3 O 4 /SiO 2 nanocomposite showed a good removal capacity for the removal of Cr(VI) ions and Congo red dye when compared to previously reported materials. However, the difference in the adsorbent efficiency between materials may be controlled by the variability of the interactions between pollutants and the material functional groups. Strong interactions with specific functional groups present on the adsorbent surface allow a high adsorption capacity [67]. Furthermore, the competitive potential application of these innovative adsorbents should be evaluated taking into consideration different parameters associated with the material characteristics (regeneration, degradation, life cycle, etc.) and with the wastes resulting from the process (loaded pollutant disposal, chemicals used for the adsorption-desorption, etc.). Moreover, a cost comparison between these materials should be conducted.

Conclusions
In this study, a promising polymer-based nanocomposite, PPy/Fe 3 O 4 /SiO 2 , was synthesized for the elimination of Congo red dye and Cr(VI) from water. The synthesized nanocomposite was characterized using different techniques (XRD, FT-IR, SEM, etc.). XRD results confirmed the crystalline structure of Fe 3 O 4 nanoparticles that decreased by the addition of PPy and silica. Additionally, SEM images confirmed the size of the synthesized materials. FT-IR bands approved the successful combination between three components of the hybrid Fe 3 O 4 , SiO 2 , and PPy. The synthesized nanocomposite was examined for the removal of Cr(VI) and Congo red dye from water. The effects of different factors including the contact time, adsorbent dosage, solution pH, and initial concentration on the adsorption process were studied to detect the optimum conditions. The adsorption data were found to be more fitting to the Langmuir model with maximum adsorption of 298.22 mg.g −1 and 361.43 mg.g −1 for the removal of Cr(VI) and Congo red, respectively. This indicated the monolayer adsorption of Cr(VI) and Congo red on the energetically homogeneous active sites of the PPy/Fe 3 O 4 /SiO 2 nanocomposite. The regeneration study indicated the ability to reuse the nanocomposite several times for the removal of Cr(VI) and Congo red, which may reduce the overall cost of the treatment. Finally, we can conclude that the PPy/Fe 3 O 4 /SiO 2 nanocomposite is a promising material for water treatment and must be examined in the future for additional pollutant removal.