This research compared two potential adsorbents for the efficient adsorption of toxic hexavalent chromium. The non-magnetic material STAC-Mt and the magnetic material FeSO4-STAC-Mt were synthesized by a simple impregnation method using montmorillonite (Mt), octadearyl dimethyl ammonium chloride (STAC) and ferrous sulfate as raw materials. The structural and morphological characteristics of both adsorbents were investigated by BET, XRD, FTIR, Zeta, VSM, TEM, SEM and XPS techniques. SEM and TEM results clearly revealed that FeSO4-STAC-Mt had a more loosely curled structure than STAC-Mt and the existence of well dispersed diamond-shaped magnetic particles. The saturation magnetization intensity of 17.949 emu/g obtained by VSM further confirmed the presence of magnetite particles in FeSO4-STAC-Mt. Due to the superparamagnetic properties of magnetite, the adsorption performance of FeSO4-STAC-Mt was better than STAC-Mt. FeSO4-STAC-Mt adsorbed up to 43.98 mg/g of Cr(VI), meanwhile it was easily separated from the reaction mixture by an external magnetic field. Intermittent adsorption studies at pH, adsorbent dosage and time revealed a rapid Cr(VI) adsorption process. In combination with response surface optimization analysis, a removal rate of 98.03% of Cr(VI) was obtained at pH 5–6. The adsorption process was properly described by the pseudo-second-order kinetic equation and the Langmuir equation, and the adsorption process was chemisorption and single molecular layer adsorption. In addition, the removal of Cr(VI) reached 72.68% after five cycles, demonstrating the good stability of the FeSO4-STAC-Mt.

  • Synthesis of magnetic nanomaterials using a simple alkaline oxidation of ferrous sulphate.

  • Prepared magnetic and non-magnetic quaternary ammonium salt modified montmorillonite for Cr(VI) adsorption.

  • The adsorption rate of FeSO4-STAC-Mt reached 98.03% and the regeneration efficiency was high at 72.68% after five cycles.

Graphical Abstract

Graphical Abstract
Graphical Abstract

Due to rapid industrialization, large amounts of toxic heavy metals have been released into the global groundwater ecosystem (Idrees et al. 2018). Chromium occurs in aquatic systems in different oxidation states with individual environmental, chemical, and biological characteristics (Hua et al. 2012). Cr(VI) is regarded as more toxic than Cr(III) because it contains a lethal dose of 80–160 mg/L (Ashour & Tony 2020). Moreover, the toxicity of Cr(VI) is easily absorbed by the body, causing damage to human liver organs and affecting the metabolic process of substances in the body (Rehman et al. 2021). Most methods are costly, infeasible and inefficient when heavy metal concentrations are 10–100 times the minimum (Zhang et al. 2021a, 2021b). Among the water treatment technologies, adsorption is one of the most successfully applied methods because it is easy to handle, simple, cost effective (Tian et al. 2022), and has strong industrial applicability compared with many other methods (Tao et al. 2019).

As a new type of clay, montmorillonite (Mt) is receiving more attention for metal removal due to its low cost, abundance, large surface area, good structural stability and high ion exchange capacity (Kang et al. 2018). Mt has the characteristics of being hydrophilic, with ultra-high swelling properties, is oleophobic and has little compatibility with polymers (Sun et al. 2016). Due to the negative charge on the surface of suspensions of Mt, original Mt usually have little or no affinity for anions and exhibit low adsorption for Cr2O72− which is electronegativity too. Thus, cationic surfactant molecules are considered to be the best component for electrostatic adsorption with clay minerals through ion exchange and electrostatic interactions. The use of quaternary ammonium salt cationic surfactant (STAC) intercalated montmorillonite not only significantly increases the organic matter content (Jemima et al. 2019), but also modifies the hydrophobic nature of the montmorillonite and improves the application of the clay in wastewater treatment. Simultaneously, STAC intercalates organic macromolecules into the clay mineral layers through exchange with inorganic cations, as well as hydrophobic bonding, increasing the montmorillonite layer spacing and changing the charge properties as well as the hydrophobic properties of the surface (Liu et al. 2019a, 2019b; Castro-Castro et al. 2020). As early as 2004, STAC-modified montmorillonite materials were synthesised by Soares et al. but the adsorption properties were not measured (Soares et al. 2004). Hong et al. used STAC-modified retortite for Cr(VI) adsorption, but had problems with low adsorption capacity and difficult separation (Hong et al. 2008). Liu et al. used STAC and ethylenediamine-modified montmorillonite to determine the adsorption properties on Cu2+ and obtained results of high adsorption, but relatively poor stability (Liu et al. 2019a, 2019b).

In recent years, magnetic (Fe3O4) particles, have received a lot of attention for pigments, magnetic resonance imaging, data storage media and magnetic drug delivery (Kalantari et al. 2014). Magnetic applications have been used in water treatment since 1873, but magnetic montmorillonite adsorbents are still a relatively new concept (Mehta et al. 2015). The introduction of magnetic particles (Fe3O4) into a sparse and porous adsorbent substrate with a large specific surface area can better improve the adsorption performance. The adsorption capacity of As(V) was enhanced by the introduction of magnetic Fe3O4 nanoparticles into wheat straw by Tian et al. (2011). The adsorption of methylene blue by Fe3O4-activated montmorillonite was investigated by Chang and colleagues who demonstrated that the composite had good stability and reproducibility (Chang et al. 2016). Jang and Lee successfully synthesised magnetite nanoparticles (MNP-OMMTs) of organically modified montmorillonite for the efficient removal of iodide (Jang & Lee 2018). These typical modified Mt materials mentioned above all exhibited efficient adsorption of contaminants and stability of the composite material. At the same time, magnetic separation technology is of great interest for its simplicity and greenness in the sorption and removal of pollutants.

We focused on the structure of the modified adsorbent. The chemical structure and porosity of montmorillonite can support the preparation of magnetic nanocomposites with excellent properties. However, the organic magnetic montmorillonite has been less studied, especially for its application for the adsorption of Cr(VI). Therefore, through STAC and inorganic iron salts modification of low-cost montmorillonite, nature-friendly, efficient, economical and easily synthesised quaternary ammonium salt-modified magnetic and non-magnetic adsorbent materials were synthesized in this study and their ability to bind Cr(VI) was evaluated. In particular, the key aspect of this study involved a simple method that was used to synthesize high particle size magnetic particles using alkali oxidation of ferrous sulfate. Finally, we also focused on the effects of wastewater pH, adsorbent dosage and contact time on the adsorption of Cr(VI) by magnetic materials.

Materials

The octadearyl dimethyl ammonium chloride (STAC, C21H46NCl) was purchased from the Tianjin Damao Chemical Reagent Plant, China. The montmorillonite (Mt) was purchased from the Zhejiang Fenghong New Material Co., China. The potassium dichromate (K2Cr2O7), ferrous sulfate (FeSO4), diphenylcarbonyl dihydrazide (C13H14N4O), hydrochloric acid (HCl), and sodium hydroxide (NaOH) were supplied by Nanjing Chemical Reagents Ltd, China. All the chemicals were of analytical grade and used without further purification.

Synthesis of materials

In this paper, surface ammonium functionalized magnetic nanoparticles were synthesized (Figure 1) using the composite modification of Mt with ferrous sulfate and octaddearyl dimethyl ammonium chloride (STAC).
Figure 1

Synthetic route of STAC-Mt and FeSO4-STAC-Mt.

Figure 1

Synthetic route of STAC-Mt and FeSO4-STAC-Mt.

Close modal

Briefly, 1.6 g of STAC was added to the Mt suspension (2% mass fraction). The suspension was stirred vigorously for 3 h using a magnetic stirrer. The precipitate was washed six times with deionised water and dried in an oven at 60 °C for 12 h. Finally, organically modified montmorillonite STAC-Mt was obtained. A certain amount of ferrous sulphate was dissolved in deionised water and this was stirred vigorously at 50 °C for 5 h with a magnetic stirrer to obtain a 0.3 M solution of ferrous sulphate. The ferrous sulphate solution was added to the STAC-Mt suspension and adjusted to pH of 11 using NaOH (0.1 M), the mixture was heated to a temperature of to 90°, stirred magnetically for 3 h, centrifuged, dried, ground and passed through a 300-mesh sieve to finally obtain FeSO4-STAC-Mt.

Physicochemical characterization

A Hitachi SU8010 modelled scanning electron microscope with an energy-dispersive X-ray analyzer was adopted to examine the surface morphology and elemental analysis of the composite. The functionalities present in the synthesized materials were investigated using Fourier-transform infrared (FTIR, IR Affinity-ISWL) spectroscopy under the transmission mode, ranging from 400 to 4,000 cm−1. The X-ray photoelectron spectroscopy (XPS) spectra of the composite before and after adsorption were studied using the Nexsa XPS System. The zeta potential of the samples was measured with a Zetasizer Nano ZS90 system (Malvern, UK). Transmission electron microscopy (TEM) was carried out at 100 kV using a Hitachi JEOL-JEM 2100F.

In order to measure the magnetic change before and after the sorbent process, a vibrating sample magnetometer (VSM) was used to measure the magnetic content of the sorbent. Thermogravimetric analysis (TG STA449F3) provided an insight into the weight loss of the adsorbent at different temperatures and facilitated the determination of the conversion of different structures and stability in the adsorbent. The test conditions were a flow rate of 50 ml/min under N2 atmosphere and a heating rate of 10 °C/min, while ramping up to 800 °C.

Cr(VI) adsorption experiments

In total, 0.2 g of modified nanocomposite was subjected to horizontal oscillation adsorption experiments with 50 mg/L potassium dichromate solution (pH = 5.0). The contact time was varied in the range 0–120 min. The pH (adjusted by 0.1 M HCl or 0.1 M NaOH) was studied in the range 2.0–12.0 to determine the optimum absorption pH. The effect of 0.05–0.3 g adsorbent dosage on the removal of Cr(VI) was investigated. It should be noted that, after each adsorption experiment, the adsorbate–adsorbent mixture was filtered through a Millipore membrane filter (0.45 μm), and the residual Cr(VI) concentration in the solution was determined using UV–Vis light (UV-4802, UNICO spectrophotometer) at a maximum wavelength λ = 540 nm. In addition, the amount of Cr(VI) (qe, mg/g) adsorbed on the STAC-Mt and FeSO4-STAC-Mt (Equation (1)) and the Cr(VI) removal percentage (Equation (2)), were calculated using the following formulas:
(1)
(2)
where qe (mg/g) is the amount of adsorbed metal ion at equilibrium, C0 and Ce (mg/L) are the initial metal ion and the metal ion concentration remaining in aqueous solution at equilibrium, respectively, V (L) is the volume of the metal solution, and m (g) is the mass of the adsorbent.

Physicochemical characterization of nanocomposite

XRD analysis

The XRD pattern (Figure 2) exposed the phase of the as-synthesized adsorbents and pristine Mt clay. The Mt samples had characteristic peaks at 5.78°, 19.7°, 35.26°, 42.5°, and 61.8 ° corresponding to (001), (211), (004), (206) and (246) crystal planes, respectively (Zheng et al. 2017; Anthony et al. 2021). At the same time, the characteristic peak at 26.74° was derived from quartz impurities, which were typical of Mt with a certain degree of crystallinity (Fatimah et al. 2021; Mekidiche et al. 2021). The formation of the FeSO4-STAC-Mt was accompanied by a marked change in the Mt structure. The main diffraction peaks of both STAC-Mt and FeSO4-STAC-Mt of the modified composites were shifted to a lower angle (Siregar et al. 2018). The (001) reflection at 5.78° represents the basal d001 of Mt spacing of 1.21 nm. After modification, the d001 diffraction peaks of the two modified samples all transferred to lower angles, and the d001 values of STAC-Mt and FeSO4-STAC-Mt were 2.00 nm and 2.03 nm, respectively. The small difference in d001 between STAC-Mt and FeSO4-STAC-Mt may be due to the fact that the size of the magnetite hydrosol was much larger than the Mt interlayer space can accommodate, resulting in magnetite particles not entering the Mt interlayer space through ion exchange (Yuan et al. 2009; Zhang et al. 2021a, 2021b). The STAC propped up the Mt which led to an increase in layer spacing and meanwhile created more adsorption sites.
Figure 2

Typical XRD pattern of Mt, STAC-Mt and FeSO4-STAC-Mt.

Figure 2

Typical XRD pattern of Mt, STAC-Mt and FeSO4-STAC-Mt.

Close modal

In Figure S1 in Supporting Information, the FeSO4-STAC-Mt diffraction peaks at 30.2°, 35.6°, 43.3°, 57.3 ° and 62.8° showed magnetite with a cubic spinel structure corresponding to the (220), (311), (400), (511) and (440) crystal planes respectively, which were all belonged to Fe3O4 (Siregar et al. 2018). Based on these data, the FeSO4-STAC-Mt was assumed as a magnetite (Fe3O4) phase which has superparamagnetic properties, and hence will facilitate in easier magnetic separation (Irawan et al. 2019). With the introduction of STAC and Fe3O4, the characteristic diffraction peaks of Mt weaken or even disappear, and these changes indicate a strong bond between Mt (Si-O-) and magnetite, which eventually makes Mt magnetic. In addition, it is also possible that this is the result of the exfoliation of the Mt lamellar structure at higher alkaline environments (Cottet et al. 2014).

SEM analysis

SEM analysed the morphological structure of the modified Mt, from which it can be seen that there were significant differences in the surface morphology of the three Mts. In Figure 3(a), the original Mt had a pronounced lamellar structure and a smooth surface, which were very consistent with previous descriptions. Figure 3(b) clearly shows that the lamellar structure of the modified Mt becomes more sparse compared to the pristine Mt, indicating that STAC successfully intercalated the lamellar montmorillonite. This was attributed to the exchange of quaternary ammonium cations in STAC and metal cations such as Na+, K+ and Mg2+ in Mt into the clay layer when STAC fully entered the Mt layer (Figure 3(b)), which eventually expanded the layer spacing.
Figure 3

SEM images of Mt (a), STAC-Mt (b,c) and FeSO4-STAC-Mt (d).

Figure 3

SEM images of Mt (a), STAC-Mt (b,c) and FeSO4-STAC-Mt (d).

Close modal

It can be observed in Figure 3(d) that the surface of FeSO4-STAC-Mt was rougher than STAC-Mt and clearly covered with Fe3O4 particles, indicating that Fe3O4 was successfully loaded on the Mt (Chen et al. 2017). This is explained by the fact that Mt (negative charge) and Fe3O4 (positive charge) are more easily bonded together by electrostatic attraction.

TEM photography of the sample (In Figure S2 in Supporting Information) showing the presence of Fe3O4 particles, indicated that the nanoparticles contained in the synthesis were clustered together and showed a rhombic structure with a nanometer size of approximately 20 nm. This suggested that magnetite particles could be loaded onto the surface of montmorillonite by a single alkaline oxidation of ferrous sulphate, giving it magnetic properties.

FTIR analysis

The possibility of surface binding with Cr(VI) was studied by FTIR analysis, and the spectra are presented in Figure 4. The position of most of the energy bands of the Mt did not change after modification by STAC, which indicated that the basic crystal structure of the modified Mt remained unaltered (Hong et al. 2008; Wu et al. 2012; Yu et al. 2019). In Figure 4(a), the IR band of Mt was observed at 3,622 cm−1, attributed to the -OH stretching vibration associated with octahedral O-Al3+ or O-Si2+. The band peak at 513 cm−1 is the Mg-O bond bending vibration (Fatimah et al. 2021). The absorption peaks at 1,003 cm−1 and 910 cm−1 represent the Si-O-Si stretching vibrations and the flexural vibrations of Al-O in the Mt lattice, respectively. The new peaks at 2,922 cm−1, 2,852 cm−1 and 1,642 cm−1 for STAC-Mt and FeSO4-STAC-Mt were caused by the stretching vibrations of symmetric and antisymmetric -CH2 and the flexural vibrations belonging to -CH2, indicating that STAC had been successfully inserted between layers of Mt (Hong et al. 2008).
Figure 4

(a) FTIR spectra of Mt, STAC-Mt and FeSO4-STAC-Mt; (b) 50–1000 cm−1 FTIR spectra of Mt, STAC-Mt and FeSO4-STAC-Mt.

Figure 4

(a) FTIR spectra of Mt, STAC-Mt and FeSO4-STAC-Mt; (b) 50–1000 cm−1 FTIR spectra of Mt, STAC-Mt and FeSO4-STAC-Mt.

Close modal

The sample FeSO4-STAC-Mt showed an increase in both the anti-symmetric peaks and symmetric stretching vibrational peaks in the methylene group at 2,922 cm−1 and 2,852 cm−1 compared with STAC-Mt. This was due to the modification of the inorganic iron salts, which enhanced the peaks at these two locations. In Figure 4(b), the attachment of Fe3O4 in the Mt structure was determined by the absorption band at 441 cm−1, representing the Fe-O symmetric stretching vibration. Here, 621 cm−1 represents Fe-O-Fe and the peak at 3,400 cm−1 is assigned to Fe-OH, which mean that Fe3O4 is loaded onto the composite modified Mt (Irawan et al. 2019; Fatimah et al. 2021). In summary, the results of FT-IR analysis confirmed the successful modification of montmorillonite by quaternary ammonium salts and magnetite.

BET analysis

The key factor in determining the adsorption capacity is the surface area of the material, as the surface area can positively determine the number of effective collisions between reactants and functional sites (Muhammad et al. 2019). Table 1 shows that the specific surface area and total pore volume of the modified adsorbent were both smaller than those of the original Mt, which were caused by the addition of STAC to create hydrogen bonding (Shoukat et al. 2017). Conversely, the subsequent loading of Fe3O4 onto the Mt led to a decrease in pore diameter (Table 1). This is probably due to the insertion of ionic species within the Mt layer spacing and the blockage of interlayer channels, confirming the successful grafting of STAC and Fe3O4 in the clay matrix (Huang et al. 2017).

Table 1

BET surface area and pore size distribution data of Mt, STAC-Mt and FeSO4-STAC-Mt composite

SampleSurface area (m2/g)Pore diameter (nm)Total pore volume (cm3/g)
Mt 29.25 13.888 0.102 
STAC-Mt 1.8622 30.634 0.012 
FeSO4-STAC-Mt 9.812 27.563 0.068 
SampleSurface area (m2/g)Pore diameter (nm)Total pore volume (cm3/g)
Mt 29.25 13.888 0.102 
STAC-Mt 1.8622 30.634 0.012 
FeSO4-STAC-Mt 9.812 27.563 0.068 

At the same time, the average pore size increased from 13.888 nm to 27.563 nm, this indicated that the modification enlarged the pore size by introducing STAC between the Mt layers. The pore channels of the Mt were blocked due to iron and STAC molecules entering between the Mt layers or being exchanged and adsorbed onto the surface of the Mt, thus making it difficult for N2 to enter the pore channels of the Mt. It can be seen from the Figure 5 that the modified adsorbent belongs to the type IV adsorption–desorption isotherm. This type of isotherm is typical of mesoporous structures (Wan et al. 2017). As the mesoporous pore channels are exposed to capillary coalescence, hysteresis lines are presented and are category B hysteresis lines. These can manifest that the original pore structure and properties of the modified Mt still exist.
Figure 5

N2 adsorption–desorption isotherms for Mt, STAC-Mt and FeSO4-STAC-Mt.

Figure 5

N2 adsorption–desorption isotherms for Mt, STAC-Mt and FeSO4-STAC-Mt.

Close modal

Zeta potential

The zeta potential measurements of Mt, STAC-Mt and FeSO4-STAC-Mt under varying pH values are shown in Figure 6. When increasing the pH from 2 to 12, the zeta potential of Mt decreased from −6.32 mV to −20.08 mV, which may be due to deprotonation of Mt surface groups or the adsorption of OH onto the Mt surface (Liu et al. 2020). Regarding the SATC-Mt samples, the positively charged surface was obtained in almost all pH ranges because the STAC cation loading reversed the Mt negatively charged surface. The zeta potential of FeSO4-STAC-Mt remained positive with the pH ranging from 2 to 10. This is due to the highly positively charged quaternary ammonium cation. The surface positive charge of FeSO4-STAC-Mt was significantly lower compared to STAC-Mt, which may have been influenced by the synthesis of magnetite on montmorillonite. During magnetite synthesis, some of the STAC+ on the surface of the STAC-Mt samples was released, which in turn led to surface charge reversal. With the increase in the pH, the adsorption of OH reduced its zeta potential but remained positive, which suggests that it is easy to remove anionic pollutants from wastewater using FeSO4-STAC-Mt and Mt and STAC-Mt.
Figure 6

Zeta potential of Mt, STAC-Mt and FeSO4-STAC-Mt.

Figure 6

Zeta potential of Mt, STAC-Mt and FeSO4-STAC-Mt.

Close modal

XPS

Figure 7(a) shows the fully measured XPS spectra of FeSO4-STAC-Mt before and after the adsorption of Cr(VI), displaying the characteristic peaks of C, N, O, Fe, Si, Al and Cr at the corresponding binding energy (BE) values. There was no significant change after FeSO4-STAC-Mt adsorption, except for a Cr2p peak at 578.06 eV (Ren et al. 2022).
Figure 7

(a) XPS spectra of Cr before and after adsorption of adsorbent FeSO4-STAC-Mt; (b) fine spectra of Cr; (c) fine spectra of Fe.

Figure 7

(a) XPS spectra of Cr before and after adsorption of adsorbent FeSO4-STAC-Mt; (b) fine spectra of Cr; (c) fine spectra of Fe.

Close modal

Figure 7(b) shows that the high resolution spectra of Cr2p had characteristic peaks at 588.97 eV (Cr2p1/2), 576.47 eV (Cr2p3/2), 585.57 eV (Cr2p1/2), and 579.07 eV (Cr2p3/2), corresponding to Cr(III) and Cr(VI), respectively. The fitting results showed that Cr(VI) and Cr(III) in FeSO4-STAC-Mt accounted for 57.85% and 42.15% of the total Cr, respectively, indicating that some Cr(VI) reduction reactions occurred during the adsorption process. The high-resolution spectrum of Fe2p showed peaks at 710–726 eV corresponding to Fe3O4 particles loaded on montmorillonite (Zheng et al. 2017). Combined with the absence of new functional groups in the FTIR spectra, it is inferred that Fe(II) reacts with Cr(VI) as an electron donor to reduce it to Cr(III).

VSM

It is assumed that the magnetite nanoparticles are well dispersed between the Mt layers, which is consistent with the SEM results. Also, the magnetisation curve (Figure 8) of this FeSO4-STAC-Mt showed a ferromagnetic behaviour, which clearly gave a saturation magnetisation intensity of 17.494 emu/g (Figure 8(a)) before adsorption. Therefore, both points indicated that the modified Mt already had strong magnetic properties (Larraza et al. 2012). The saturation magnetisation intensity of FeSO4-STAC-Mt after adsorption of Cr(VI) was 17.718 emu/g (Figure 8(b)), which clearly shown that the saturation magnetisation intensity had not changed much and was still magnetic. Experiments have shown that magnetised sorbents exhibited extremely high water dispersion under stirring conditions, which helped to better maintain adsorbent–adsorbate interactions resulting in improving sorption performance.
Figure 8

Magnetic hysteresis curves before (a) and after (b) FeSO4-STAC-Mt and STAC-Mt adsorption.

Figure 8

Magnetic hysteresis curves before (a) and after (b) FeSO4-STAC-Mt and STAC-Mt adsorption.

Close modal

TG-DTA

The thermogravimetric and differential thermal analysis (TG-DTA) curves of the adsorbent FeSO4-STAC-Mt in air are presented in Figure 9. The curves of FeSO4-STAC-Mt showed exothermic peaks at 170 °C, 300 °C and 430 °C, corresponding to the evaporation of physical adsorption of water, desorption of crystalline water and insufficient degradation of STAC at lower temperatures (210–500 °C), resulting in carbonization of STAC at higher temperatures, respectively caused by weight loss of 4.6%, 10.9% and 16.67%. In addition, weight loss of FeSO4-STAC-Mt was slight before 200 °C, so the adsorbent FeSO4-STAC-Mt was structurally stable and performed well at less than 200 °C.
Figure 9

TG-TGA patterns of FeSO4-STAC-Mt.

Figure 9

TG-TGA patterns of FeSO4-STAC-Mt.

Close modal

Evaluation of adsorption performance

Effect of modified Mt on Cr(VI) adsorption

As can be seen from Figure 10, Mt, STAC-Mt and FeSO4-STAC-Mt performed adsorption of K2Cr2O7 to simulate the removal of Cr(VI) from the wastewater. The adsorption experiment was carried out by selecting 0.2 g of each of the three adsorbents and adding them to 50 mg/L of chromium-containing wastewater for determination. The absorbance of the samples was measured within 0–120 min to determine the concentration of chromium after adsorption. The removal rate of Cr(VI) by FeSO4-STAC-Mt can reach 96.82%. The reason may be that the ferric ions in ferrous sulphate replace the cations on the surface of Mt or the loading of ferric tetroxide onto the surface of Mt under alkaline conditions, which increases the number of active sites, thus the removal rate of FeSO4-STAC-Mt is more effective. As Cr(VI) is generally present in aqueous solutions as anions such as HCrO4 and Cr2O72−, the original Mt is negatively charged in aqueous solution and exerts electrostatic repulsion on the anions in water. Therefore, the removal rate of virgin Mt is lower.
Figure 10

Removal rates of Cr(VI) by adsorbents Mt, STAC-Mt and FeSO4-STAC-Mt.

Figure 10

Removal rates of Cr(VI) by adsorbents Mt, STAC-Mt and FeSO4-STAC-Mt.

Close modal

Effect of different pH on the removal rate of Cr(VI)

Figure 11 shows the removal rate of adsorbed Cr(VI) and the amount per unit adsorption for solutions with different pH. The experimental protocol was to select 50 mg/L of chromium-containing wastewater, adjust the desired solution pH using 0.1M NaOH or HCl, then add 0.2 g of adsorbent to the different pH solutions for adsorption experiments. The graphs revealed that the removal rate of Cr(VI) showed an increasing trend when the pH was in the range of 2.0–6.0 and a decreasing trend in the range of 6.0–12.0. It reached maximum adsorption of 23.474 mg/g at pH of 6.0. At pH 2.0–6.0, dichromate (Cr2O72−) and chromate hydrogen (HCrO4) ions were the major species in solution. At low pH, the nitrogen atoms in the adsorbent were protonated to attract the Cr(VI) anion, which in turn replaced the doped chloride. The presence of large amounts of H+ in solution influences the charge distribution on the adsorbent surface. Some of these absorbing metal functional groups separate, allowing the chloride ion to compete with the chromium anion for adsorption. As the pH increases from 2 to 6, there is less and less Cl in solution and the adsorption competition between Cl and Cr2O72− or HCrO4 becomes weaker, leading to a gradual increase in the adsorption rate. When the pH value slowly is increased, the chromium ions in solution are stored in the form of chromate ions (CrO42−), and the OH ions in solution increase, which creates competition with CrO42− for adsorption, resulting in a significant reduction in the adsorption effect. Therefore, the optimum adsorption pH value was chosen to be 6.0.
Figure 11

Effect of different pH on Cr(VI) unit adsorption volume by adsorbent FeSO4-STAC-Mt.

Figure 11

Effect of different pH on Cr(VI) unit adsorption volume by adsorbent FeSO4-STAC-Mt.

Close modal

Effect of different dosages of adsorbent on the removal of Cr(VI)

In this investigation, the solution pH of the chromium-containing wastewater was 5.7. As the amount of FeSO4-STAC-Mt added increases (Figure 12), the number of active adsorption sites also increases, so the absorption rate gradually increases. However, when too much FeSO4-STAC-Mt is added, many of the active sites are occupied and the adsorption rate no longer increases. The optimum amount of FeSO4-STAC-Mt is 0.2 g, which is economical for environmental reasons.
Figure 12

Removal of Cr(VI) by different dosages of FeSO4-STAC-Mt.

Figure 12

Removal of Cr(VI) by different dosages of FeSO4-STAC-Mt.

Close modal

Adsorption isotherm

The adsorption was carried out at pH = 6 with a mechanical stirrer and took intermediate samples. The absorbance of the supernatant was measured at reaction times of 1 min, 3 min, 5 min, 8 min, 10 min, 15 min, 20 min, 25, 40 and 60 min to calculate the concentration of Cr(VI) and the experiment was repeated three times. The STAC-Mt and FeSO4-STAC-Mt Cr adsorptions were fitted by the Langmuir and Freundlich equations and the results are shown in Figure 13.
Figure 13

Fitting of the Langmuir adsorption isotherm equation to FeSO4-STAC-Mt (a) and Freundlich isotherm equation to FeSO4-STAC-Mt (b).

Figure 13

Fitting of the Langmuir adsorption isotherm equation to FeSO4-STAC-Mt (a) and Freundlich isotherm equation to FeSO4-STAC-Mt (b).

Close modal
The Langmuir isotherm is represented by Equation (3):
(3)
where Ce is the concentration of Cr(VI) (mg/L) at equilibrium, qe is the adsorption capacity (mg/g), qm is the maximum capacity of the adsorbent (mg/g) and KL is the Langmuir constant (L/mg):
(4)

In the Langmuir isotherm equation, the dimensionless constant-separation factor RL (Equation (4)) can be used as a measure of whether an adsorption process can occur thermodynamically. When 0 < RL < 1, it means that the adsorption reaction can occur.

At the same time, the Freundlich isotherm model is expressed as Equation (5):
(5)
where qe is the adsorption capacity (mg/g), Ce is the concentration of Cr(VI) at equilibrium (mg/L), and KF and n are the Freundlich constant and the dimensionless constant, respectively:
(6)
where lnqe (Equation (6)) is the vertical coordinate and lnCe is the horizontal coordinate, a linear fit was performed. If the linear relationship is well established, when 0.1 < 1/n < 1, it indicates that the reaction is easy to carry out.

The Langmuir (Figure 13(a)), Freundlich (Figure 13(b)) adsorption isotherm model are used to explore the nature and mechanism of adsorption. Figure 13 compiles the results of the isothermal study as well as the results of the Langmuir and Freundlich linear fits for FeSO4-STAC-Mt. The isothermal parameters derived from the linear plots are listed in Table 2.

Table 2

FeSO4-STAC-Mt adsorption Cr(VI) kinetic parameters

SampleLangmuir
Freundlich
qmKLR2ln KF1/nR2
FeSO4-STAC-Mt 36.5065 1.8408 0.99973 3.12361 0.20104 0.89434 
SampleLangmuir
Freundlich
qmKLR2ln KF1/nR2
FeSO4-STAC-Mt 36.5065 1.8408 0.99973 3.12361 0.20104 0.89434 

Experimental data yielded maximum sorption values that were close to the qm obtained from the Langmuir isotherm model. The qm values obtained by linear fitting of the Langmuir model were 36.5065 mg/L. These results indicate that the adsorption was monomolecular layer adsorption and the values obtained were 1/n < 1, indicating that the adsorption was feasible (Irawan et al. 2019; Ain et al. 2020). This showed that the incorporation of cationic surfactants with multifunctional groups and the impregnation of magnetic nanoparticles were responsible for the excellent adsorption performance of the modified clay minerals, respectively. Conversely, the ultra-high swelling properties and extraordinary hydrophilicity of the modified Mt were also responsible for its enhanced adsorption capacity.

Adsorption kinetics

Adsorption kinetics is an important parameter for understanding the mechanism of Cr(VI) adsorption on adsorbent surfaces. In this study, the experimental data were further evaluated by using two kinetic models, pseudo-first-order and pseudo-second-order models, respectively (Haounati et al. 2021).

The pseudo-first-order dynamics model (Equation (7)) and the pseudo-second-order dynamics model (Equation (8)) are formulated as follows:
(7)
(8)
where: qe (mg/g) is the adsorption capacity at equilibrium; qt (mg/) is the amount of adsorption at time t. t (min) is the adsorption reaction time; K1 (min−1) and k2 (min−1) are the pseudo-first and pseudo-second order reaction rates respectively.
The fitted first-order and fitted second-order kinetic models were fitted to FeSO4-STAC-Mt, and the fitted results are shown in Table 3 and Figure 14. The proposed primary reaction kinetic model of FeSO4-STAC-Mt was a poor fit to the experimental data (Figure 14(a)) and the proposed secondary reaction kinetic model was a good fit to the experimental data (Figure 14(b)) (R2 > 0.999), implying that the proposed secondary reaction kinetic model was more suitable for describing the entire reaction process of Cr(VI) in aqueous solution on modified Mt. Furthermore, it is apparent that there is a large error between the equilibrium adsorption capacity obtained during the fitting of the quasi-first-order adsorption kinetics and our experimentally measured qe, whereas the adsorption capacity calculated by the quasi-second-order adsorption kinetics is close to the experimental value. The formation of chemical bonds is the main factor affecting the quasi-secondary kinetic adsorption, and it can be inferred that the adsorption process is mainly chemisorption (Huang et al. 2019; Liao et al. 2020). Therefore, the proposed second-order adsorption kinetics is more suitable for describing the adsorption process.
Table 3

Kinetic parameters of Cr(VI) adsorption by FeSO4-STAC-Mt

SamplePseudo-first-order
Pseudo-second-order
qe (mg/g)K1 (min−1)R2qe (mg/g)K2 (min−1)R2
FeSO4-STAC-Mt 7.673 0.020557 0.78749 23.474 0.02184 0.99992 
SamplePseudo-first-order
Pseudo-second-order
qe (mg/g)K1 (min−1)R2qe (mg/g)K2 (min−1)R2
FeSO4-STAC-Mt 7.673 0.020557 0.78749 23.474 0.02184 0.99992 
Figure 14

Proposed first-order (a) and proposed second-order (b) kinetic equation fitting for the reaction of FeSO4-STAC-Mt adsorbed Cr(VI).

Figure 14

Proposed first-order (a) and proposed second-order (b) kinetic equation fitting for the reaction of FeSO4-STAC-Mt adsorbed Cr(VI).

Close modal

RSM

Response surface methodology (RSM) is considered to be an effective condition for analysing complex response conditions. The analysis was carried out using response surfaces in three dimensions to observe the correlation between the three factors mentioned above over the range of the experiment. Figure 15 shows the response surface 3D plots. From Figure 15 it can be seen that the curves exhibit an upward convex shape and that extreme value points can be found, indicating that the horizontal range was chosen reasonably well. All three factors can be seen to be significant in Table S1 of the supplementary material, indicating that all three factors have some influence on the adsorption of Cr(VI). In this paper, numerical optimisation was carried out by the direct search method and the optimum adsorption conditions were optimised for a time of 79 min, a pH of 5.3 and an adsorbent dosage of 0.22 g. The optimised best response value of 98.95% was obtained. Finally, three validation experiments were conducted to judge the optimisation results and the average removal rate obtained was 98.03%. The results showed a very good agreement between the predicted response experiments and the actual values.

Regeneration of adsorbent and adsorption mechanism

In this work, the adsorbent was attached with magnetic properties, which can be easily recovered in regenerative use, further realizing the economic and efficient utilization of the adsorbent. The Cr(VI) adsorbed FeSO4-STAC-Mt was weighed in a beaker, and NaOH (0.1 M) eluents were added into it, soaked for 5 h–8 h, washed, filtered and dried to make regenerated adsorbent. The reason for choosing NaOH is that when sodium hydroxide is used as the eluent, chromium ions will react with hydroxide ions to form a chromium hydroxide precipitate and, if the hydroxyl concentration is high, chromium ions will continue to react with hydroxide ions to form Cr(OH)4 and Cr(OH)4 can be dissolved in water and easily desorbed from the adsorbent surface, thus improving the cycle efficiency. NaCl (0.1 M) and HCl (0.1 M) were also used as eluents for comparison with NaOH.

The initial adsorption efficiency of FeSO4-STAC-Mt for Cr(VI) was 96.82%, as shown in Figure 16. The adsorption efficiency of FeSO4-STAC-Mt on Cr(VI) was 30.69%, 72.68% and 27.35% after five regeneration cycles with hydrochloric acid, sodium hydroxide and sodium chloride as the eluent, respectively. The adsorption efficiency of FeSO4-STAC-Mt for Cr(VI) remained high and constant after five regeneration cycles of the adsorbent when sodium hydroxide was used as the eluent.
Figure 15

Response surface 3D plots showing the effects of time (A), pH (B) and dosage (C) on Cr(VI) removal rates. (a) Effects of A and C on Cr(VI) removal rate. (b) Effects of A and B on Cr(VI) removal rate. (c) Effects of B and C on Cr(VI) removal rate.

Figure 15

Response surface 3D plots showing the effects of time (A), pH (B) and dosage (C) on Cr(VI) removal rates. (a) Effects of A and C on Cr(VI) removal rate. (b) Effects of A and B on Cr(VI) removal rate. (c) Effects of B and C on Cr(VI) removal rate.

Close modal
Figure 16

Adsorption efficiency of Cr(VI) on FeSO4-STAC-Mt regeneration times.

Figure 16

Adsorption efficiency of Cr(VI) on FeSO4-STAC-Mt regeneration times.

Close modal
Firstly, the zeta potential characterisation described above confirms the surface positive charge nature of FeSO4-STAC-Mt, which allows the removal of Cr anions by electrostatic gravitation. Secondly, Cl was incorporated into STAC in the form of counter ions and due to its high mobility, the adsorption of Cr(VI) was promoted by an ion exchange mechanism, as shown in Equation (9). Finally, the presence of 42.15% Cr (III) and 57.85% Cr(VI) on the FeSO4-STAC-Mt surface after adsorption can be found using the XPS technique, indicating that Cr(VI) in solution has been adsorbed onto the surface of the adsorbent and then reduced to Cr(III) through a non-homogeneous redox process. Therefore, it can be inferred that the magnetite on FeSO4-STAC-Mt has the ability to reduce Cr(VI) to Cr (III). Thus, the mechanism of Cr(VI) removal by FeSO4-STAC-Mt is mainly physicochemical, including electrostatic gravitation, ion exchange and redox:
(9)

This study demonstrates the feasibility of using STAC-Mt and FeSO4-STAC-Mt as adsorbents for the removal of chromium from simulated waste water solutions. The following conclusions were drawn from this study.

  • FeSO4-STAC-Mt, a magnetic organic composite material synthesised using alkaline ferrous sulphate oxide, achieved up to 98.03% removal of Cr(VI) and performed better than STAC-Mt.

  • XRD demonstrated that the composite modification increased the layer spacing of the modified montmorillonite from 1.26 nm to 2.03 nm. SEM and TEM clearly showed the loose structure of the modified montmorillonite and well dispersed diamond-shaped magnetic particles.

  • The average pore size increased from 13.888 nm to 27.563 nm, it indicated that the modification expanded the pore size by introducing STAC between the Mt layers. Zeta potential indicated that two of the modified adsorbents exhibited positively charged nature and had significant adsorption effect on chromium anion.

  • It was shown that the maximum adsorption of chromium by FeSO4-STAC-Mt was 43.98 mg/g at pH = 6, and the amount of adsorbent was 0.2 g.

  • The Langmuir isotherm is most consistent with the monomolecular layer adsorption of chromium by FeSO4-STAC-Mt. Also, the adsorption of Cr on FeSO4-STAC-Mt is consistent with quasi-secondary adsorption kinetics indicating that the process is chemisorption.

  • Desorption experiments showed that the adsorption of Cr(VI) on FeSO4-STAC-Mt using NaOH eluent (0.1 M) decreased to less than 72.68% after five adsorption–desorption cycles. This demonstrates that magnetic particle composites are easy to separate and are stable.

This work was supported by the key research and development program of Shaanxi, China (2018GY-067).

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

Ain
Q. U.
,
Rasheed
U.
,
Yaseen
M.
,
Zhang
H.
, He, R. & Tong, Z.
2020
Fabrication of magnetically separable 3-acrylamidopropyltrimethylammonium chloride intercalated bentonite composite for the efficient adsorption of cationic and anionic dyes
.
Applied Surface Science
514
,
145929
.
https://doi.org/10.1016/j.apsusc.2020.145929
.
Anthony
E. T.
,
Alfred
M. O.
,
Saliu
T. D.
&
Oladoja
N. A.
2021
One-pot thermal synthesis of Ceria/Montmorillonite composite for the removal of hexavalent chromium from aqueous system
.
Surfaces and Interfaces
22
,
100914
.
https://doi.org/10.1016/j.surfin.2020.100914
.
Ashour
E. A.
&
Tony
M. A.
2020
Eco-friendly removal of hexavalent chromium from aqueous solution using natural clay mineral: activation and modification effects
.
SN Applied Sciences
2
(
12
),
1
13
.
https://doi.org/10.1007/s42452-020-03873-x
.
Castro-Castro
J. D.
,
Macías-Quiroga
I. F.
,
Giraldo-Gomez
G. I.
&
Sanabria-González
N. R.
2020
Adsorption of Cr(VI) in aqueous solution using a surfactant-modified bentonite
.
The Scientific World Journal
2020
.
https://doi.org/10.1155/2020/3628163
.
Chang
J.
,
Ma
J.
,
Ma
Q.
,
Zhang
D.
, Qiao, N., Hu, M. & Ma, H.
2016
Adsorption of methylene blue onto Fe3O4/activated montmorillonite nanocomposite
.
Applied Clay Science
119
,
132
140
.
https://doi.org/10.1016/j.clay.2015.06.038
.
Chen
H.
,
Li
Y.
,
Wang
S.
&
Zhou
Y.
2017
Synthesis of montmorillonite/Fe3O4-OTAB composite capable of using as anisotropic nanoparticles
.
Applied Surface Science
402
,
384
391
.
https://doi.org/10.1016/j.apsusc.2017.01.103
.
Cottet
L.
,
Almeida
C. A. P.
,
Naidek
N.
,
Viante
M. F.
, Lopes, M. C. & Debacher, N. A.
2014
Adsorption characteristics of montmorillonite clay modified with iron oxide with respect to methylene blue in aqueous media
.
Applied Clay Science
95
,
25
31
.
https://doi.org/10.1016/j.clay.2014.03.023
.
Fatimah
I.
,
Citradewi
P. W.
,
Fadillah
G.
,
Sahroni
I.
, Purwiandono, G. & Dong, R.-a.
2021
Enhanced performance of magnetic montmorillonite nanocomposite as adsorbent for Cu (II) by hydrothermal synthesis
.
Journal of Environmental Chemical Engineering
9
(
1
),
104968
.
https://doi.org/10.1016/j.jece.2020.104968
.
Haounati
R.
,
Ouachtak
H.
,
El Haouti
R.
,
Akhouairi
S.
, Largo, F., Akbal, F., Benlhachemi, A., Jada, A. & Addi, A. A.
2021
Elaboration and properties of a new SDS/CTAB@Montmorillonite organoclay composite as a superb adsorbent for the removal of malachite green from aqueous solutions
.
Separation and Purification Technology
255
,
117335
.
https://doi.org/10.1016/j.seppur.2020.117335
.
Hong
H.
,
Jiang
W.-T.
,
Zhang
X.
,
Tie
L.
& Li, Z.
2008
Adsorption of Cr(VI) on STAC-modified rectorite
.
Applied Clay Science
42
(
1
),
292
299
.
https://doi.org/10.1016/j.clay.2008.01.015
.
Hua
M.
,
Zhang
S.
,
Pan
B.
,
Zhang
W.
, Lv, L. & Zhang, Q.
2012
Heavy metal removal from water/wastewater by nanosized metal oxides: a review
.
Journal of Hazardous Materials
211–212
,
317
331
.
https://doi.org/10.1016/j.jhazmat.2011.10.016
.
Huang
Z.
,
Li
Y.
,
Chen
W.
,
Shi
J.
, Zhang, N., Wang, X., Li, Z., Gao, L. & Zhang, Y.
2017
Modified bentonite adsorption of organic pollutants of dye wastewater
.
Materials Chemistry and Physics
202
,
266
276
.
https://doi.org/10.1016/j.matchemphys.2017.09.028
.
Huang
H.
,
He
D.
,
Tang
Y.
,
Guo
Y.
, Li, P., Qv, W., Deng, F. & Lu, F.
2019
Adsorption of hexavalent chromium from an aqueous phase by hydroxypropyl methylcellulose modified with diethylenetriamine
.
Journal of Chemical & Engineering Data
64
(
1
),
98
106
.
https://doi.org/10.1021/acs.jced.8b00607
.
Idrees
N.
,
Tabassum
B.
,
Abd_Allah
E. F.
,
Hashem
A.
, Sarah, R. & Hashim, M.
2018
Groundwater contamination with cadmium concentrations in some West U.P. Regions, India
.
Saudi Journal of Biological Sciences
25
(
7
),
1365
1368
.
https://doi.org/10.1016/j.sjbs.2018.07.005
.
Irawan
C.
,
Nata
I. F.
&
Lee
C.-K.
2019
Removal of Pb (II) and As (V) using magnetic nanoparticles coated montmorillonite via one-pot solvothermal reaction as adsorbent
.
Journal of Environmental Chemical Engineering
7
(
2
),
103000
.
https://doi.org/10.1016/j.jece.2019.103000
.
Jemima
W. S.
,
Magesan
P.
,
Chiranjeevi
P.
&
Umapathy
M. J.
2019
Sorption properties of organo modified montmorillonite clay for the reclamation of chromium (VI) from waste water
.
Silicon
11
(
2
),
925
933
.
https://doi.org/10.1007/s12633-018-9887-z
.
Kalantari
K.
,
Ahmad
M. B.
,
Shameli
K.
,
Hussein
M. Z. B.
, Khandanlou, R. & Khanehzaei, H.
2014
Size-controlled synthesis of Fe3O4 magnetic nanoparticles in the layers of montmorillonite
.
Journal of Nanomaterials
2014
,
739485
.
https://doi.org/10.1155/2014/739485
.
Kang
S.
,
Zhao
Y.
,
Wang
W.
,
Zhang
T.
, Chen, T., Yi, H., Rao, F. & Song, S.
2018
Removal of methylene blue from water with montmorillonite nanosheets/chitosan hydrogels as adsorbent
.
Applied Surface Science
448
,
203
211
.
https://doi.org/10.1016/j.apsusc.2018.04.037
.
Larraza
I.
,
López-Gónzalez
M.
,
Corrales
T.
&
Marcelo
G.
2012
Hybrid materials: Magnetite–Polyethylenimine–Montmorillonite, as magnetic adsorbents for Cr(VI) water treatment
.
Journal of Colloid and Interface Science
385
(
1
),
24
33
.
https://doi.org/10.1016/j.jcis.2012.06.050
.
Liao
H.
,
Li
Y.
,
Li
H.
,
Li
B.
, Zhou, Y., Liu, D. & Wang, X.
2020
Efficiency and mechanism of amidoxime-modified X-type zeolite (AO-XZ) for Cs+ adsorption
.
Chemical Physics Letters
741
,
137084
.
https://doi.org/10.1016/j.cplett.2019.137084
.
Liu
X.
,
Zhou
F.
,
Chi
R.
,
Feng
J.
, Ding, Y. & Liu, Q.
2019a
Preparation of modified montmorillonite and its application to rare earth adsorption
.
Minerals
9
(
12
),
747
.
https://doi.org/10.3390/min9120747
.
Liu
Y.
,
Luan
J.
,
Zhang
C.
,
Ke
X.
& Zhang, H.
2019b
The adsorption behavior of multiple contaminants like heavy metal ions and p-nitrophenol on organic-modified montmorillonite
.
Environmental Science and Pollution Research
26
(
10
),
10387
10397
.
https://doi.org/10.1007/s11356-019-04459-w
.
Liu
S.
,
Chen
M.
,
Cao
X.
, Li, G., Zhang, D., Li, M., Meng, N., Yin, J. & Yan, B.
2020
Chromium (VI) removal from water using cetylpyridinium chloride (CPC)-modified montmorillonite
.
Separation and Purification Technology
241
,
116732
.
https://doi.org/10.1016/j.seppur.2020.116732
.
Mehta
D.
,
Mazumdar
S.
&
Singh
S. K.
2015
Magnetic adsorbents for the treatment of water/wastewater – a review
.
Journal of Water Process Engineering
7
,
244
265
.
https://doi.org/10.1016/j.jwpe.2015.07.001
.
Mekidiche
M.
,
Khaldi
K.
,
Nacer
A.
,
Boudjema
S.
, Ameur, N., Lerari-Zinai, D., Bachari, K. & Choukchou-Braham, A.
2021
Organometallic modified montmorillonite application in the wastewater purification: pollutant photodegradation and antibacterial efficiencies
.
Applied Surface Science
569
,
151097
.
https://doi.org/10.1016/j.apsusc.2021.151097
.
Muhammad
Y.
,
Rashid
H. U.
,
Subhan
S.
,
Rahman
A. U.
, Sahibzada, M. & Tong, Z.
2019
Boosting the hydrodesulfurization of dibenzothiophene efficiency of Mn decorated (Co/Ni)-Mo/Al2O3 catalysts at mild temperature and pressure by coupling with phosphonium based ionic liquids
.
Chemical Engineering Journal
375
,
121957
.
https://doi.org/10.1016/j.cej.2019.121957
.
Rehman
A. U.
,
Nazir
S.
,
Irshad
R.
,
Tahir
K.
, Rehman, K. ur., Islam, R. U. & Wahab, Z.
2021
Toxicity of heavy metals in plants and animals and their uptake by magnetic iron oxide nanoparticles
.
Journal of Molecular Liquids
321
,
114455
.
https://doi.org/10.1016/j.molliq.2020.114455
.
Ren
B.
,
Jin
Y.
,
Zhao
L.
,
Cui
C.
& Song, X.
2022
Enhanced Cr(VI) adsorption using chemically modified dormant Aspergillus niger spores: process and mechanisms
.
Journal of Environmental Chemical Engineering
10
(
1
),
106955
.
https://doi.org/10.1016/j.jece.2021.106955
.
Shoukat
S.
,
Bhatti
H. N.
,
Iqbal
M.
&
Noreen
S.
2017
Mango stone biocomposite preparation and application for crystal violet adsorption: a mechanistic study
.
Microporous and Mesoporous Materials
239
,
180
189
.
https://doi.org/10.1016/j.micromeso.2016.10.004
.
Siregar
S. H.
,
Wijaya
K.
,
Kunarti
E. S.
&
Syoufian
A.
2018
Synthesis and characteristics of the magnetic properties of Fe3O4–(CTAB-montmorillonite) composites, based on variation in Fe3+/Fe2+ concentrations
.
Oriental Journal of Chemistry
34
(
2
),
716
.
https://doi.org/10.13005/ojc/340213
.
Soares
V.
,
Nascimento
R.
,
Menezes
V.
&
Batista
L.
2004
TG characterization of organically modified montmorillonite
.
Journal of Thermal Analysis and Calorimetry
75
(
2
),
671
676
.
https://doi.org/10.1023/b:jtan.0000027161.10803.60
.
Sun
L.
,
Ling
C. Y.
,
Lavikainen
L. P.
,
Hirvi
J. T.
, Kasa, S. & Pakkanen, T. A.
2016
Influence of layer charge and charge location on the swelling pressure of dioctahedral smectites
.
Chemical Physics
473
,
40
45
.
https://doi.org/10.1016/j.chemphys.2016.05.002
.
Tao
E.
,
Ma
D.
,
Yang
S.
,
Sun
Y.
, Xu, J. & Kim, E. J.
2019
Zirconium dioxide loaded montmorillonite composites as high-efficient adsorbents for the removal of Cr3+ ions from tanning wastewater
.
Journal of Solid State Chemistry
277
,
502
509
.
https://doi.org/10.1016/j.jssc.2019.07.002
.
Tian
Y.
,
Wu
M.
,
Lin
X.
,
Huang
P.
& Huang, Y.
2011
Synthesis of magnetic wheat straw for arsenic adsorption
.
Journal of Hazardous Materials
193
,
10
16
.
https://doi.org/10.1016/j.jhazmat.2011.04.093
.
Tian
B.
,
Zhang
R.
,
Chen
T.
,
Wang
G.
, Liu, S. Chen, Z. & Hu, J.
2022
Phenanthroline-based microporous organic materials for removal of Cu (II) from aqueous solution and reutilization of spent adsorbent as catalysts
.
Water Science and Technology
.
https://doi.org/10.2166/wst.2022.218
Wan
D.
,
Wang
G.
,
Li
W.
&
Wei
X.
2017
Investigation into the morphology and structure of magnetic bentonite nanocomposites with their catalytic activity
.
Applied Surface Science
413
,
398
407
.
https://doi.org/10.1016/j.apsusc.2017.03.265
.
Wu
P.
,
Dai
Y.
,
Long
H.
,
Zhu
N.
, Li, P., Wu, J. & Dang, Z.
2012
Characterization of organo-montmorillonites and comparison for Sr(II) removal: equilibrium and kinetic studies
.
Chemical Engineering Journal
191
,
288
296
.
https://doi.org/10.1016/j.cej.2012.03.017
.
Yu
P.
,
Wang
Z.
,
Lai
P.
,
Zhang
P.
& Wang, J.
2019
Evaluation of mechanic damping properties of montmorillonite/organo-modified montmorillonite-reinforced cement paste
.
Construction and Building Materials
203
,
356
365
.
https://doi.org/10.1016/j.conbuildmat.2019.01.110
.
Yuan
P.
,
Fan
M.
,
Yang
D.
,
He
H.
, Liu, D., Yuan, A., Zhu, J. & Chen, T.
2009
Montmorillonite-supported magnetite nanoparticles for the removal of hexavalent chromium [Cr(VI)] from aqueous solutions
.
Journal of Hazardous Materials
166
(
2
),
821
829
.
https://doi.org/10.1016/j.jhazmat.2008.11.083
.
Zhang
X.
,
Song
Z.
,
Dou
Y.
,
Xue
Y.
, Ji, Y., Tang, Y. & Hu, M.
2021a
Removal difference of Cr(VI) by modified zeolites coated with MgAl and ZnAl-layered double hydroxides: efficiency, factors and mechanism
.
Colloids and Surfaces A: Physicochemical and Engineering Aspects
621
,
126583
.
https://doi.org/10.1016/j.colsurfa.2021.126583
.
Zhang
H.
,
Xu
H.
,
Xia
M.
,
Wang
F.
& Wan, X.
2021b
The adsorption and mechanism of benzothiazole and 2-hydroxybenzothiazole onto a novel ampholytic surfactant modified montmorillonite: experimental and theoretical study
.
Advanced Powder Technology
32
(
4
),
1219
1232
.
https://doi.org/10.1016/j.apt.2021.02.022
.
Zheng
X.
,
Dou
J.
,
Yuan
J.
,
Qin
W.
, Hong, X. & Ding, A.
2017
Removal of Cs+ from water and soil by ammonium-pillared montmorillonite/Fe3O4 composite
.
Journal of Environmental Sciences
56
,
12
24
.
https://doi.org/10.1016/j.jes.2016.08.019
.
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Supplementary data