Introduction

A water problem is being caused by the industry’s current production of a lot of different forms of wastewater that contain dangerous chemicals [1,2,3,4,5,6,7,8]. Due to urbanization and industrialization, the world’s ground water has become a severe issue. The wastewater must be treated before being released into the environment in order to avoid water pollution [9,10,11,12,13,14]. Several model organisms have been exposed to dyes, which has led to genotoxic and mutagenic effects [12, 15,16,17]. There are many methods used to remove dyes from wastewater including filtration, precipitation, adsorption, photodegradation, and chemical degradation [12, 18,19,20,21,22]. The dye compounds are classified as irritants and have adverse effects on humans, including respiratory distress, lacrimation, skin irritation, and carcinogenic consequences. The majority of synthetic dyes provide significant health risks to living systems by altering the chemical and physical properties of soil, the aquatic environment, and the flora and fauna. This causes the natural environment to collapse [23,24,25,26,27,28,29].

Nanotechnology has become a cutting-edge, state-of-the-art technology in recent years, with applications in every aspect of human life. Researchers have focused on creating nanoparticles and numerous techniques have been developed to achieve this goal [12, 30,31,32,33,34,35]. Finding a new solution to the problems that are now being encountered in the field of environmental technology has had an effect on people's daily lives [24, 36]. The remarkable properties of metal nanoparticles including their thermal, catalytic, mechanical, optical and magnetic capabilities, have made a scientific study of them alluring [37,38,39,40,41]. These distinctive characteristics are the fallout of a high surface area to volume ratio, and high surface energy contrived through nanoparticles. Metal nanoparticles are widely used in a variety of fields, including optics, electronics, material science, and the biological and medical sciences [24, 42, 43].

Iron oxide nanoparticles are getting more and more interest in the field of drug delivery and magnetic resonance imaging (MRI) because of their unique superparamagnetic properties, flexibility, low-cytotoxicity, and biocompatibility [44,45,46,47]. Many efforts are being made to produce iron oxide nanoparticles for both their vital uses across a range of fields and their fundamental scientific interest. Due to their magnetic properties, high surface area, and small size, the usage of iron oxide-based nanomaterial with unique properties and functionality is now being explored extensively [44, 48,49,50]. Iron oxide-based magnetic nanoparticles are used in a number of scientific, industrial, and medicinal fields [51, 52]. Nevertheless, an essential step in conjunction with such applications is the surface modification of iron oxide nanoparticles using various functionalization techniques [53,54,55].

Polyelectrolyte multilayers adsorbed on iron oxide nanoparticles are very significant for shielding against NPs degradation, modification of surface charge and for changing magnetization features of magnetic cores because of their interaction with polymers [56, 57]. The well-known layer-by-layer (LbL) technique, which allows for the nanoscale tailoring of the chemical and physical properties of multilayered materials, can be used to create polyelectrolyte multilayers on charged substrates [58, 59]. Additionally, the use of this technique causes a surface charge reversal [60, 61], which is determined by electrostatic interactions between the polyelectrolyte chains, solvent and substrate, which are highly influenced by factors including temperature, pH, ionic strength, and species concentration [62,63,64], particularly in the situation of weak polyelectrolytes like poly(allylamine hydrochloride) (PAH). Nevertheless, when the multilayer of polyelectrolyte simply involves electrostatic interactions, the rise in entropy caused by counter ion release to the bulk is the driving force for self-assembly [65, 66]. Additionally, the strong cooperatively between polymer chains (and eventually, the structure of the multilayer) will depend on the type of polymers utilized in the LbL process. In addition, the following interactions must be considered: interactions between donors and acceptors, steric interactions, hydrogen bonds, hydration interactions, covalent bonds, cycles of adsorption and drying, stereocomplex formation, or specific recognition. The surface charge of the nanoparticle is altered by these interactions, which also affects the stability of colloidal suspensions in solutions [67].

In the current study, we created iron oxide nanoparticles using the precipitation method at two calcination temperatures (200 and 500 °C). The essential benefits of the precipitation method are its high production and the low minimum temperature requirement, which prevents the formation of big grains. We also describe the production of iron oxide nanoparticles, their characterisation, and surface modifications utilizing two polyelectrolytes. Here, we investigate how the adsorption and photocatalytic activity of Fe2O3NPs with FSS dye is influenced by surface coatings consisting of anionic poly(sodium 4-styrenesulfonate) (PSS) and cationic poly(allylamine hydrochloride) (PAH) polyelectrolytes as shown in Fig. 1. In order to remove FSS dye from synthetic dye solutions, we investigate the photocatalytic and adsorption properties of both free Fe2O3NPs and surface-modified Fe2O3NPs. Fluorescein dye was quickly and successfully removed from an aqueous solution using surface-modified Fe2O3NPs. The ability of the Fe2O3NPs to electrostatically attach to fluorescein dye depends on the surface charge of the particles. Here, we are investigating the possibility that covering the Fe2O3NPs with an exterior layer of a cationic polyelectrolyte will improve their photocatalytic and adsorption activity, whereas covering them with an exterior layer of anionic polyelectrolyte may decline their photocatalytic and adsorption activity because of electrostatic repulsion from the negatively charged fluorescein dye. The multilayer coverings offer excellent surface coverage and the external PAH layer offers superior photocatalytic and adsorption activity for fluorescein dye. To the best of our knowledge, no research has been done on the application of this type of modification for Fe2O3NPs made using the LbL technique and employed for the photocatalytic and adsorption of fluorescein dye. Here, we show for the first time that surface-modified Fe2O3NPs exhibit improved and preferred photocatalytic and adsorption activity for the FSS dye as compared to unmodified Fe2O3NPs.

Fig. 1
figure 1

A Schematic diagram showing the coating of bare Fe2O3NPs with two consecutive layers of anionic PSS and cationic PAH polyelectrolytes. B Schematic diagram showing the adsorption of FSS dye on bare and surface modified Fe2O3NPs

Results and discussion

Characterization of Fe2O3NPs

The size and morphology of synthesized Fe2O3NPs were examined by TEM analysis. TEM examination was performed to get clear information about shape, size, and structural details. Figure 2A–F shows the TEM images of Fe2O3NPs that were produced using the precipitation method and calcined for 4 h at 200 and 500 ℃. The average particle diameter of the Fe2O3NPs after a 4 h heat treatment was determined to be 48 ± 10 nm at 200 ℃ (Fig. 2A–C) and 96 ± 7 nm at 500 ℃ (Fig. 2D–F). It is evident that nanoparticles are primarily found in nature as granules with small and big spherical shaped particles. The calcination temperature utilized in the synthesis of Fe2O3NPs has a significant impact on the nanoparticle size. The TEM images of Fe2O3NPs were proved that the particle size increased with the increase of the calcination temperature (Fig. 2A–F).

Fig. 2
figure 2

TEM images of Fe2O3NPs at lower and higher magnifications prepared with different calcination temperatures. A–C calcined at 200 ℃ and D–F calcined at 500 ℃. G FTIR spectrum of Fe2O3 uncalcined and calcined at 200 and 500 ℃ produced by precipitation method. H The impact of the calcination temperature during the Fe2O3NPs synthesis on the BET surface area of Fe2O3NPs from 80 to 500 ℃

The BET technique was used to measure the surface areas of Fe2O3NPs formed from Fe2O3 at different temperatures. Note that the Fe2O3NPs surface area declined as the calcination temperature increased from 199 m2 g−1 at 80 °C to 27 m2 g−1 at 500 ℃ as shown in Fig. 2H. FTIR spectroscopy was used to further confirm the production of Fe2O3 nanoparticles. Figure 2G displays FTIR spectra of Fe2O3 uncalcined and calcined at 200 and 500 ℃ formed by using the precipitation method. The significant absorption peaks at 443 and 556 cm−1 for the uncalcined Fe2O3 nanoparticles product can be attributed to the vibrations of the Fe–O band [68, 69]. The very broad absorption band centered at 3398 cm−1 and reaching peak at 1638 cm−1 is attributed to the stretching and bending vibrations of the hydroxyl groups and/or water molecules, respectively [70]. The results show that the products were prepared in an aqueous solution, which resulted in the presence of structural hydroxyl groups as well as a minor quantity of absorbed water on their surface. FTIR spectrum analyses of pure Fe2O3 nanoparticles calcined at 200 and 500 ℃ generated by precipitation method displays the reduction of bands related to the hydroxyl group. We also observed the appearance of two bands at 434 and 527 cm−1 that can be related to the Fe–O bond of Fe2O3NPs [71]. The characteristic peak at 434 and 527 cm−1 becomes very strong for Fe2O3 nanoparticles calcined at 200 and 500 ℃, indicating the creation of the stretching mode of Fe2O3. Figure S5A–C shows the Fe2O3NPs powder’s X-ray diffraction patterns. Figure S5A displays the sample’s XRD pattern before annealing, while Fig. S5B and C show the XRD pattern after annealing. The XRD results in Fig. S5A–C demonstrate that as the calcination temperature is raised, the intensity and half-height breadth of the diffraction peak steadily decrease, resulting in an increase in crystal size. Using the Scherrer equation, the range of average crystallite sizes found in the XRD data was 4–16 nm. It was discovered as a result that altering the calcination temperature resulted in a change in the crystallite size of pure Fe2O3NPs. An Energy Dispersive X-ray Diffraction (EDX) analysis was also carried out to confirm the elemental composition of the generated Fe2O3NPs. It was found that the iron and oxygen signals are present in the Fe2O3NPs sample, according to the EDX results in Fig. S5D.

To study the formation of each polyelectrolyte layer deposited on the Fe2O3NPs, the zeta potential and hydrodynamic diameter experiments were measured by DLS. We coated two additional layers of PSS and PAH to cover Fe2O3NPs that were 70 nm at 200 ℃ and 95 nm at 500 ℃ using the methods described above [33, 64]. Figure 3A, B displays that the coated Fe2O3NPs size increases after each additional polyelectrolyte coating because of partial aggregation. The variation of zeta potential with the polyelectrolyte layer number for PSS and PAH coatings are presented in Fig. 3C, D. The zeta potential of the Fe2O3NPs changed from a positive charge to a negative charge for Fe2O3NPs/PSS due to PSS single layer being a negatively charged. An additional PAH coating produced positively charged Fe2O3NPs/PSS/PAH with zeta potentials of + 42 mV (Fig. 3C) and + 31 mV (Fig. 3D). Adding the polyelectrolyte layer with the opposing charge causes the particle surface charge to alternate, as expected.

Fig. 3
figure 3

A and B The particle size and C and D zeta potential of bare-and polymer-modified Fe2O3NPs calcined at 200 and 500 °C as a function of PSS and PAH layers. The free Fe2O3NPs are represented by the zero layers. PSS deposition is represented by layer number 1 and PAH deposition is represented by layer number 2

FSS dye adsorption and photocatalytic studies  

The effect of the amount of Fe2O3NPs on FSS dye adsorption

We investigated the photocatalytic and adsorption properties of Fe2O3NPs toward FSS dye under UV irradiation as well as in dark conditions. Different Fe2O3NPs adsorbent amounts including 0.05 g, 0.1 g, 0.15 g, 0.2 g, 0.25 g, and 0.3 g were utilized to evaluate the effects of nanoparticle amounts calcined at 200 and 500 ℃ in the removal of FSS dye. The works were carried out in 100 cm3 solution of 10 mg dm−3 initial FSS concentration at room temperature. The percentage of FSS dye adsorption and photodegradation efficiency increased with increasing doses of Fe2O3NPs as illustrated in Fig. 4 and Fig. S3. This was explained by the fact that as the amount of adsorbent increases, there is a higher chance that the FSS dye will come into touch with the available active sites of the Fe2O3NPs. As an anionic dye model, FSS dye was used in the present research to evaluate how well Fe2O3NPs removed FSS dyes in both dark and light conditions. This result could be attributed to the anionic dye being electrostatically attracted to cationic Fe2O3NPs, which causes the FSS dye to be absorbed by Fe2O3NPs. After adsorption of 0.05 g of Fe2O3NPs with 10 mg dm−3 of FSS dye, there was a noticeable difference in FSS dye removal in dark (Fig. 4C and Fig. S3C) and UV light conditions (Fig. 4D and Fig. S3D) because of the photoactivity of the Fe2O3NPs. FSS dye quickly adsorbs to Fe2O3NPs at first, but the adsorption activity gradually slows and reaches equilibrium after 10 min under UV light and darkness, as illustrated in Fig. 4 and Fig. S3. The rate of adsorption varies quickly since all of the adsorbent sites are initially empty. The decrease in the number of unoccupied adsorbent sites and the dye concentration over time cause the adsorption rate to become low. The decreased rate of adsorption indicates that FSS probably formed a monolayer on the surface of the Fe2O3NPs. As a consequence, once equilibrium is reached, there aren’t enough free active sites, therefore more absorption is required. The removal percentage of FSS dye that was adsorbed by Fe2O3NPs calcined at 200 and 500 ℃ in both light and dark was reported. Figure 4 and Fig. S3 show that the removal percentage of FSS dyes using Fe2O3NPs under UV light is higher than that in the dark at the same conditions. One probable description is that aqueous suspensions of Fe2O3NPs under UV light can produce ROS like O2●− and H2O2 [64]. The decolorization of dyes is widely discussed in the literature review. The hydroxyl radicals are generated in a solution that acts as an oxidant, which is formed on Fe2O3NPs. Furthermore, when water molecules on the surface of Fe2O3NPs interact with holes (h+ (VB)), hydroxyl ion radicals are generated. Therefore, hydroxyl ion radicals destroy the FSS dye [17, 27]. The results represented in Fig. S3 show that the Fe2O3NPs calcined at 500 ℃ have lower adsorption and photocatalytic activity on FSS dye when compared to the Fe2O3NPs calcined at 200 ℃ (Fig. 4). One possible explanation is that the increase of the calcination temperature leads to an increase of size of Fe2O3NPs. Thus, the smallest size was obtained at the lowest calcination temperature (200 ℃). It was also found that the Fe2O3NPs surface area increased as the calcination temperature declined as described above.

Fig. 4
figure 4

The impact of Fe2O3NPs amount calcined at 200 ℃ on the removal percentage and photodegradation efficiency of FSS dye under (A and C) dark conditions and (B and D) UV light

Effect of initial FSS dye concentration

One of the most significant aspects affecting the adsorption process may be the initial dye concentration since it indirectly impacts the effectiveness of dye removal by lowering or raising the number of binding sites on the adsorbent surface. The effectiveness of dye removal and the maximum amount of dye bound in equilibrium in such systems of water treatment are strongly related to the initial dye concentration [72]. By changing the initial concentration of the FSS dye over a wide range (5–50 mg dm−3), the impact of the initial concentration on the removal percentage and photodegradation efficiency was examined. Adsorption and photocatalytic tests were conducted at various initial FSS dye concentrations of FSS dye at a fixed pH and 0.2 g of Fe2O3NPs. The results in Fig. 5 and Fig. S4 show that the removal percentage and photodegradation efficiency of FSS dye decreased with increasing the initial FSS dye concentration. The saturation of adsorption sites on the adsorbent surface can explain for this phenomenon. In this situation, as the initial FSS dye concentration increases, so does the ability of the adsorbent, which is because of the high mass transfer driving force at high initial FSS concentrations. The initial FSS dye concentration of the solute drives the adsorption process by favoring mass transfer and diffusion from the solution (which contains a higher amount of FSS dye) to the adsorbent's free surface [72]. At higher initial FSS dye concentrations, the total free adsorption sites are limited, which could result in a decrease in the removal percentage of FSS dye. The rise at higher initial FSS dye concentrations could be attributed to increased driving forces. On the other hand, because the ratio of active sites to FSS dye molecules can be high at low concentrations, all molecules can interact with the adsorbent and are nearly immediately removed from the solution [72]. We also examined the adsorption and photocatalytic activity of bare Fe2O3NPs toward various concentrations of FSS dye upon illumination with UV light compared with that under dark conditions to assess the influence of the oxidative stress owing to the reactive oxygen species (ROS). The data in Fig. 5 and Fig. S4 show that there was a remarkable difference between the removal percentage of FSS dye in dark conditions (Fig. 5C) and that under UV light (Fig. 5D) because of the photoactivity of the Fe2O3NPs. One possible explanation is that under UV irradiation, electrons in the VB may be stimulated to the CB of the oxide, with the concomitant creation of the same quantity of holes in the VB, resulting in the creation of an electron–hole pair. Redox reactions with organics can then result from further charge separation and the migration of the created charge carriers toward the surface of the catalyst. In terms of redox potentials, reducing the fluorescent dye can occur at potential (E0 ≈ − 0.34 V vs. Ag/AgCl). On another hand, the valence band of iron oxide is located at 2.5 V and its conduction band is located at 0.4 V, this means that it is comparable to the reduction of FSS by CB of iron oxide [73]. Direct oxidation of the FSS dye to reactive intermediates is possible due to the high oxidative potential of the hole (h+) (VB) in the Fe2O3NPs. Another way that water might decompose is to produce hydroxyl radicals, which are extremely reactive. On the other hand, a more effective reaction will occur when electrons interact with dissolved oxygen molecules to form superoxide radical anions, which then protonate to become hydroperoxyl radicals (HO2) and lastly OH radicals [71].

Fig. 5
figure 5

Effect of initial concentration on the removal percentage and photodegradation efficiency of FSS dye under (A and C) dark conditions and (B and D) UV light in the presence of Fe2O3NPs calcined at 200 ℃

Kinetics and adsorption isotherms of FSS dye adsorption on Fe2O3NPs

The kinetics of FSS adsorption on Fe2O3NPs was studied. At room temperature, batch systems were used for all experimental tests. Kinetic studies are crucial in the field of adsorption because they shed light on the adsorption mechanism. The adsorption ability and rate constant of a Fe2O3NPs substance used as an adsorbent must be higher. In this work, pseudo-first- and second-order kinetics was used. The perfectly matched plots of the adsorption kinetic model are shown in Fig. 6A, B. First-order kinetic graphs for the FSS dye are shown in Fig. 6A, whereas second-order kinetic plots are shown in Fig. 6B. We discovered that the correlation coefficient of the pseudo-second-order model was significantly higher than that of the pseudo-first-order model (Table S1). Additionally, it was observed that the pseudo-second-order model’s plotted simulated adsorption capacity had a better fit with the data than the pseudo-first-order model's estimated adsorption capacity (see Fig. 6A, B). Thus, the pseudo-second-order model provides the most accurate description of the adsorption mechanism for FSS dye on Fe2O3NPs. The kinetic parameters for FSS dye on Fe2O3NPs obtained from the plots in Fig. 6A, B are given in Table S1. The interaction between adsorbate particles and adsorbents can be predicted using the isotherm models, which offer useful information. Applying the Langmuir and Freundlich linear isotherm models, the mechanism of FSS dye adsorption onto Fe2O3NPs was investigated. Figure 6C displays the Langmuir isotherms of FSS dye on Fe2O3NPs, whereas Fig. 6D displays the Freundlich isotherm models. These models were used to determine the maximum adsorption abilities of FSS dye on Fe2O3NPs. It was found that adsorption isotherms of FSS dye adsorption on Fe2O3NPs show good agreement with the Langmuir isotherm model. We use the calculated n values of the Freundlich model to illustrate the heterogeneities on the surface of Fe2O3NPs (Fig. 6D). In cases where n is more than 1, equal to 1, or less than 1, adsorption will be physical, linear, or chemical, respectively. The FSS dye has n values higher than 1 as shown in Fig. 6E, which in our study suggests that the absorption is physical absorption [17].

Fig. 6
figure 6

Kinetics and adsorption isotherms of FSS dye adsorption on Fe2O3NPs. A Pseudo-first-order model and B pseudo-second-order model for FSS dye. Adsorption isotherms for FSS dye on Fe2O3NPs according to C Langmuir and D Freundlich isotherm models

Adsorption and photocatalytic activity of polyelectrolyte-coated Fe2O3NPs toward FSS dye

We studied the adsorption and photocatalytic activity of Fe2O3NPs that were coated with multilayers of polyelectrolytes on FSS dye. We functionalized Fe2O3NPs with PSS and PAH and compared their FSS dye removal percentage and photodegradation efficiency with that of the bare Fe2O3NPs in dark and UV light. The aqueous solution of 10 mg dm−3 FSS dye were mixed with 0.2 g of Fe2O3NPs/PSS and Fe2O3NPs/PSS/PAH suspensions at various time for up to one hour. The results represented in Figs. 7A, C and 8A, C show that the anionic Fe2O3NPs/PSS have a lower adsorption and photocatalytic activity toward FSS dye when compared to the cationic bare Fe2O3NPs (see Fig. 4). The same treatment with the cationic Fe2O3NPs/PSS/PAH showed significant adsorption and photocatalytic activity toward FSS dye as shown in Figs. 7B, D and 8B, D. One can conclude that, by coating the Fe2O3NPs with an outer layer of anionic polyelectrolyte, their removal percentage and photodegradation efficiency is significantly decreased because of the electrostatic repulsion between the anionic Fe2O3NPs/PSS and the anionic surface of FSS dye. On the other hand, after coating Fe2O3NPs/PSS with an additional layer of PAH which reverses the particles surface charge from negative to positive. The positive surface charge of the Fe2O3NPs/PSS/PAH had a high influence on the removal percentage and photodegradation efficiency of FSS dye. The results indicate that these cationic nanoparticles Fe2O3NPs/PSS/PAH were even more effective for the removal of FSS dye than the bare Fe2O3NPs both under UV light and dark as shown in Figs. 7B, D and 8B, D. This formula of alternating adsorption and photocatalytic activity of the polyelectrolyte-coated Fe2O3NPs seems to be linked to their surface charge and the corresponding electrostatic adhesion to the negatively charged FSS dye. The data display that the cationic nanoparticles (the free Fe2O3NPs and Fe2O3NPs/PSS/PAH) have much higher removal percentage and photodegradation efficiency than their anionic form Fe2O3NPs/PSS.

Fig. 7
figure 7

The removal percentage and photodegradation efficiency of FSS dye on polyelectrolyte-coated Fe2O3NPs synthesized after annealing of Fe2O3 at 200 ℃ toward FSS dye. The removal percentage of 10 mg dm−3 FSS dyes after mixing for up to 1 h with A, C 0.2 g of Fe2O3NPs/PSS and B, D Fe2O3NPs/PSS/PAH at room temperature

Fig. 8
figure 8

The removal percentage and photodegradation efficiency of FSS dye on polyelectrolyte-coated Fe2O3NPs synthesized after annealing of Fe2O3 at 500 ℃ toward FSS dye. The removal percentage of 10 mg dm−3 FSS dyes after mixing for up to 1 h with A, C 0.2 g of Fe2O3NPs/PSS and B, D Fe2O3NPs/PSS/PAH at room temperature

Figure 9A–D summarizes the effect of free PSS, free PAH, bare Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH on the removal percentage and photodegradation efficiency of 10 mg dm−3 FSS dye under the same conditions of 0.2 g particle dose for 1 h in dark and UV light. This result indicated that the bare Fe2O3NPs and Fe2O3NPs/PSS/PAH have a strong effect on the removal of FSS dye both in dark and under UV light. This influence can be described with the positive particle surface charge leading to a strong electrostatic attraction between the cationic surface of the bare Fe2O3NPs and Fe2O3NPs/PSS/PAH and the anionic surface of the FSS dye. The data in Fig. 9A, C, D show that the presence of Fe2O3NPs/PSS/PAH has a much higher impact on the FSS dye removal percentage in dark, and UV light conditions than that of the bare Fe2O3NPs, as the adhesion of the latter to the FSS dye is driven mainly by electrostatic forces. The results confirm that free PSS and free PAH on FSS dye have a negligible adsorption and photocatalytic activity on the FSS dye, whereas Fe2O3NPs/PSS have some low level of effect compared with the uncoated Fe2O3NPs and Fe2O3NPs/PSS/PAH. This is most likely due to the electrostatic repulsion between Fe2O3NPs/PSS and FSS dye as both have negatively charged surfaces in aqueous media which leads to a decrease in the removal percentage and photodegradation efficiency of FSS dye on Fe2O3NPs/PSS.

Fig. 9
figure 9

Comparison of the effect of free PSS, free PAH, free Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH on the removal percentage and photodegradation efficiency of FSS dye in A, C dark and B, D UV light for 1 h. 10 mg dm−3 of FSS dye was mixed with the 0.2 g of nanoparticles synthesized after annealing of Fe2O3 at A, B 200 ℃ and C, D 500 ℃

We also investigated the adsorption of Reactive Red 2 dyes (RR2) as a real pollutant dye on free Fe2O3NPs and polyelectrolyte-coated Fe2O3NPs. In order to evaluate the RR2 dye removal% of free Fe2O3NPs and Fe2O3NPs functionalized with PSS and PAH were used. The aqueous solution of 70 mg dm−3 RR2 dye were mixed with 0.2 g of Fe2O3NPs, Fe2O3NPs/PSS and Fe2O3NPs/PSS/PAH suspensions at various time for up to 1 h. The data in Figs. S7 and S9 (Supporting Information) demonstrate that the anionic Fe2O3NPs/PSS has lower adsorption for the RR2 dye than the cationic bare Fe2O3NPs (see Fig. S6). The same treatment with the cationic Fe2O3NPs/PSS/PAH displayed significant adsorption with RR2 dye as presented in Figs. S8 and S9. According to the results in Figs. S8 and S9, it was found the cationic nanoparticles Fe2O3NPs/PSS/PAH were even more effective at removing RR2 dye than bare Fe2O3NPs and anionic Fe2O3NPs/PSS.

Separation of a mixture of dyes

Bare and surface modified Fe2O3NPs were employed to selectively separate different organic dyes because of their distinct and quick adsorption action towards FSS dye. The separation performance of unmodified and surface-modified Fe2O3NPs was tested using FSS/crystal violet (CV) dye mixtures in an aqueous solution with various charge states. Free Fe2O3NPs and Fe2O3NPs/PSS/PAH are designed to eliminate anionic FSS dye from the mixed solution, whilst Fe2O3NPs/PSS may be able to remove cationic CV dye. Digital photos of the dye mixture of FSS and CV before and after adsorption with free Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH were taken, as shown in Fig. 10B, D, F. The colors of the dye mixture were then compared to those of the two separate (Fig. 10A) aqueous solutions of FSS/CV dyes. The color of the mixture of yellow FSS and blue-violet CV dyes changed to brown after being mixed as shown in Fig. 10A. The dye mixture solution's color changed from brown to blue-violet after 1 h of adsorption, fitting the color of the pure CV aqueous solution (Fig. 10B, F). Nearly all of the FSS dye was absorbed by the Fe2O3NPs and Fe2O3NPs/PSS/PAH (Fig. 10C, G). On the other hand, the Fe2O3NPs/PSS effectively absorbed all of the CV dyes (Fig. 10E), changing the color of the dye combination solution from brown to yellow (Fig. 10D), which matched the color of the pure FSS aqueous solution. The concentrations of FSS and CV in the mixture solution were determined using UV–Vis spectra before and after 1 h of adsorption with unmodified and surface-modified Fe2O3NPs, as shown in Fig. 10B, D, F. According to UV–Vis spectra measured after 1 h, Fe2O3NPs and Fe2O3NPs/PSS/PAH absorbed between 85 and 98% of the FSS, whereas only a mere 10% of the CV. This demonstrates that the dye mixture can be successfully separated using Fe2O3NPs and Fe2O3NPs/PSS/PAH by selectively adsorbing FSS from the dye mixture. These results can be explained by the reduced adsorption Fe2O3NPs and Fe2O3NPs/PSS/PAH to the CV dye because of electrostatic repulsion and the better particle-dye adsorption due to electrostatic interaction when cationic Fe2O3NPs and Fe2O3NPs/PSS/PAH are combined with anionic FSS dye.

Fig. 10
figure 10

Schematic diagram showing the selective removal and adsorption of Fe2O3NPs, Fe2O3NPs/PSS, Fe2O3NPs/PSS/PAH with FSS/CV dye. A Photo of FSS/CV mixture solutions. UV–Vis spectra of FSS/CV mixture solutions before and after adsorption on the B bare Fe2O3NPs; D Fe2O3NPs/PSS; F Fe2O3NPs/PSS/PAH. Photos inside Fig. B, D, F show the FSS/CV mixture solutions before adsorption and after adsorption. C FSS dye loaded Fe2O3NPs; E CV dye loaded Fe2O3NPs/PSS; G FSS dye loaded Fe2O3NPs/PSS/PAH

Regeneration and reuse of used bare and surface modified Fe2O3NPs

In practical applications, an adsorbent's ability to be reused sustainably is important. As a result, the reuse and regeneration of the utilized Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH were also assessed for 5 cycles adsorption/desorption and the results are displayed in Fig. 11A. The desorption of FSS dye was achieved by putting the loaded FSS-nanoparticles for 3 h in 0.01 N NaOH, followed by washing five times with deionized water as shown in Fig. 11B–G. The electrostatic attraction between the Fe2O3NPs and Fe2O3NPs/PSS/PAH and the anionic FSS dye was decreased as expected as a result of deprotonating. Fe2O3NPs and Fe2O3NPs/PSS/PAH show high removal efficiency after five cycles of adsorption–desorption. As the number of reuse cycles increased, the FSS dye removal effectiveness declined; nonetheless, both the unmodified and surface-modified Fe2O3NPs lost approximately 5% of their initial efficiency over the course of five cycles. Consequently, the decline in removal effectiveness may be brought on by the changing of the surface properties of the unmodified and surface-modified Fe2O3NPs throughout the adsorption–desorption processes [17]. These results demonstrate that both the uncoated and surface-coated Fe2O3NPs are highly recyclable, making them an economical material with promising water treatment applications.

Fig. 11
figure 11

A Reusability of bare and surface modified Fe2O3NPs for the removal of FSS dye. Regeneration of used B Fe2O3NPs C Fe2O3NPs/PSS/PAH and D Fe2O3NPs/PSS by NaOH. Washing of E Fe2O3NPs F Fe2O3NPs/PSS/PAH and G Fe2O3NPs/PSS by water to reuse

Conclusion

Here we explored and discussed the mechanisms by which bare and surface modified Fe2O3NPs attack FSS dye. In this study, we used the precipitation method to produce Fe2O3NPs at two calcination temperatures (200 and 500 ℃). The effects of changes in the calcination temperature used in the synthesis of Fe2O3NPs at the level of size and morphology were discovered. TEM, FTIR, BET, and DLS techniques were used to characterize the synthesized Fe2O3NPs. The data of the various techniques display that the increase of the calcination temperature leads to an increase of size of Fe2O3NPs. In summary, the lowest calcination temperature (200 ℃) resulted in the smallest size (48 nm). The adsorption of FSS dye onto bare and surface modified Fe2O3NPs and its photocatalytic activity were then studied. Our present work indicates that bare Fe2O3NPs had significant adsorption and photocatalytic activity against FSS dye and their impact increased upon increasing the Fe2O3NPs dose. To analyze the adsorption process, the kinetics of FSS dye adsorption was investigated. The results showed that the kinetic data worked well with the pseudo-second-order kinetic model. The Langmuir isotherm model was found to best fit the adsorption equilibrium results for FSS dye adsorption. To evaluate the influence of the surface coating, a series of Fe2O3NPs coated with polyelectrolytes using the layer by-layer technique were synthesized and their adsorption and photocatalytic activity toward FSS dye was compared to that of the bare Fe2O3NPs. It was discovered that the adsorption and photocatalytic activity of the surface-modified Fe2O3NPs alternates with the particle surface charge. The nanoparticles of anionic surface (Fe2O3NPs/PSS) had much lower adsorption and photocatalytic activity than the ones of cationic surfaces (Fe2O3NPs/PSS/PAH and bare Fe2O3NPs). In general, free Fe2O3NPs and Fe2O3NPs/PSS/PAH showed remarkable adsorption and photocatalytic activity and demonstrated high efficiency against the FSS dye, even at low particle amounts. It has been observed that small amounts of cationic nanoparticles (Fe2O3NPs/PSS/PAH and bare Fe2O3NPs) have been found to remove FSS dye with efficiencies greater than 95%. This effect can be explained by the positive surface charge of the particles, which causes a strong electrostatic attraction between the anionic surface of the FSS dye and the cationic surface of the bare Fe2O3NPs and Fe2O3NPs/PSS/PAH. Our results provide new insights about the influence of the Fe2O3NPs surface coatings with polyelectrolytes using the layer by-layer technique on their adsorption and photocatalytic action and could potentially lead to development of better adsorption and photocatalytic activity formulations. It was also found that the anionic FSS dye has much higher adsorbed selectively on the Fe2O3NPs/PSS/PAH and free Fe2O3NPs adsorbent than the cationic ones. The study also showed that bare and surface modified Fe2O3NPs presented high recyclability performance and thus they will be low-cost materials and have superior probability in the treatment of water.

Materials and methods

Materials 

Iron oxide nanoparticles were synthesized using iron trichloride hexahydrate (FeCl3‧6H2O) provided by Sigma-Aldrich and ammonium hydroxide (NH4OH) was bought from Fisher Scientific. Fluorescein dye was gotten from Sigma-Aldrich. Anionic polyelectrolyte (PSS, average MW of 70 kDa) and cationic polyelectrolyte (PAH, average MW of 15 kDa) were obtained from Sigma-Aldrich, UK.

Methods 

Synthesis of iron oxide nanoparticles

The direct precipitation method was used for the synthesis of Fe2O3NPs from NH4OH as a precipitating agent and FeCl3‧6H2O as a precursor. The first step was to dissolve 4 g of FeCl3‧6H2O in 100 cm3 of distilled water under stirring at room temperature. Then, a 50 cm3 aqueous solution of 2 M NH4OH solution was added dropwise to the FeCl3‧6H2O solution under stirring. The resulting black dispersion was heated for 3 h at 80 ℃ while being continuously stirred at room temperature to produce a brown powder. The resulting sediment was collected by centrifugation at 6000 rpm and washed three times with ethanol and distilled water and finally dried at 80 ℃ as shown in Fig. S1. The final product was cooled to room temperature and calcined at (200 and 500 ℃) for 4 h [74]. All the formed nanoparticles were characterized separately, for their morphology, structural, surface properties, and chemical composition. For this purpose various techniques were used, such as Transmission Electron Microscopy (TEM), Fourier Transform Infrared (FTIR), BET, dynamic light scattering (DLS), and UV–Vis Spectrophotometer.

Preparation of polyelectrolyte-coated Fe2O3NPs

Polyelectrolyte-coated Fe2O3NPs were prepared using Fe2O3NPs synthesized after annealing of Fe2O3 at 200 and 500 ℃. The first step was to disperse 2.5 g of Fe2O3NPs in 25 cm3 of distilled water with sonication for 30 min at room temperature. Fe2O3NPs dispersion was added dropwise to an equal volume of 2.5 g in 25 cm3 anionic polyelectrolyte PSS solution in 1 mM NaCl. The samples were homogenized for 1 h on an orbital shaker, and then the excess PSS was removed by centrifuging them for 1 h at 8000 rpm after being rinsed three times with distilled water. The zeta potential distributions and particle size of the Fe2O3NPs/PSS particles were measured after they had been resuspended in 25 cm3 of distilled water. The Fe2O3NPs/PSS suspension was added dropwise into 2.5 g in 25 cm3 of cationic polyelectrolyte PAH solution that was dissolved in 1 mM NaCl to create PAH-coated Fe2O3NPs. The formed nanoparticles was shaken for 1 h and centrifuged three times for 1 h at 8000 rpm to create Fe2O3NPs/PSS/PAH [64]. The zeta potential and particle size of the surface-functionalized Fe2O3NPs (with PSS and PAH) were measured by dynamic light scattering.

Adsorption and photocatalytic experiments

The adsorption ability of the uncoated and surface-coated Fe2O3NPs to adsorb dye was examined using FSS dye. A UV–Vis spectrophotometer with a 490 nm setting was used to record the experimental results. Firstly, uncoated Fe2O3NPs and surface-coated Fe2O3NPs were prepared and mixed with 100 cm3 of FSS dye solutions. The solutions were regularly shaken for 60 min in the dark using a platform shaker as shown in Fig. S2A. We measured the absorbance at the maximum absorption wavelength both before and after adsorption. The removal percentage (R%) of FSS dye on uncoated and surface-coated Fe2O3NPs was calculated by batch adsorption experiment, that consisted of placing 100 cm3 solution of 10 mg dm−3 of FSS dye with 0.2 g of bare and surface-coated Fe2O3NPs in conical flasks. The free Fe2O3NPs and surface-coated Fe2O3NPs with FSS were gently shaken in the dark at 25 ± 5 ℃ till they reached equilibrium. The shaker speed was set at 230 rpm. Equations (1, 3, and 4) in the Supporting Information were used to calculate the FSS removal% and the amount of FSS adsorbed per unit mass of adsorbent at equilibrium Qe (mg g−1) and at a specific time Qt [17].

We also examined the photodegradation activity of FSS dye with bare Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH in the presence of light. Four 15 W mercury lamps from Philips (CLEO), Poland, were used in the photocatalytic experiment, which was carried out in a photochemical reactor. The uncoated and surface-coated Fe2O3NPs were irradiated with FSS in conical flasks using a platform shaker as presented in Fig. S2B. In all of the photodegradation experiments, 0.2 g of uncoated and surface-coated Fe2O3NPs was suspended in 100 cm3 of an aqueous solution of FSS dye. After illumination, 3 cm3 of the reaction suspension was taken, and the bare Fe2O3NPs, Fe2O3NPs/PSS, and Fe2O3NPs/PSS/PAH were extracted by spinning the mixture for 15 min at 4000 rpm in a centrifuge. A second centrifugation was found to be necessary to separate out small bare and surface-coated Fe2O3NPs particles [17]. After the second centrifugation, the absorbance of FSS at 490 nm was recorded. The photodegradation efficiency (PDE) of FSS was also calculated according to Eq. (2) in the Supporting Information.