Lan
Yang
,
Qiyuan
Lu
,
Xiao
Zhou
,
Tao
Yang
and
Chunfang
Du
*
College of Chemistry and Chemical Engineering, Inner Mongolia University, Hohhot, Inner Mongolia 010021, P. R. China. E-mail: cedchf@imu.edu.cn; Fax: +86-471-4994375; Tel: +86-471-4994375
First published on 17th July 2025
Adsorption is an effective strategy for treating water pollution and natural clay mineral-based materials exhibit great potential for removing pollutants from wastewater. In this paper, halloysite nanotubes (HNTs) modified with ethylenediaminetetraacetic acid (EDTA) were thermally treated to serve as supports for loading SnS2 to construct SnS2/HNTs(C) (SHCx-y). Methylene blue (MB) was selected as a target pollutant to examine the removal efficiency of the obtained adsorbents. SHC0.04-500 could remove more than 90% of MB (50 mg L−1) within 18 min, which was 9 and 18 times higher than those of SnS2 and HNTs(C)-500, respectively. Moreover, the adsorbent SHC0.04-500 with good pH and temperature adaptability exhibited excellent adsorption performance toward cationic dyes and various antibiotics. The adsorption process of MB over SHC0.04-500 matched well with the Langmuir isotherm and the pseudo-first-order kinetic model. The adsorption mechanism investigation suggested that the carbon layer on HNTs made the surface of SHC0.04-500 more negative, which mostly contributed to the improved adsorption performance. This work provides a low-cost, environmentally friendly, and efficient adsorbent for removing pollutants from wastewater and contributes a new strategy to enhance the removal efficiency by a simple modification method.
At present, there are multiple available techniques for treating water pollutants, including photocatalytic degradation, Fenton reaction, adsorption and so on. The degradation process refers to the breaking of a large organic dye structure into small molecules, which may produce toxic or harmful chemicals if the degradation is insufficient.7–10 Compared to degradation, adsorption has received much attention because of its simplicity, low cost, safety, and non-toxicity.11 A large number of adsorbents such as biochar, graphene oxide, and MOF composites have been applied in the removal of organic pollutants.12–14 However, the specific surface area and porosity of the above adsorbents are generally affected by the raw materials and preparation conditions, leading to an uncontrollable adsorption efficiency.15 Natural clay minerals have the advantages of large specific surface area, stable structure, and easy modification. It has been reported that the combination of minerals and adsorbents can overcome the shortcomings mentioned above and be a potential strategy for water pollution treatment.16,17 Halloysite nanotubes (HNTs) are composed of curled silicate layers with a hollow tubular morphology.18 The inner and outer walls of HNTs are composed of alumina octahedra and silica-oxygen tetrahedra, respectively, both of which contain a certain number of hydroxyl groups.19 This structural characteristic indicates that the chemical modification of HNTs could be easily achieved. Moreover, HNTs have a rich porous structure, a large specific surface area, a high aspect ratio, and low cost.20,21 In recent years, the application of HNTs in water treatment has been further explored. For instance, HNTs modified with (3-aminopropyl) triethoxysilane (H-APTES) exhibited excellent removal efficiencies toward both Cu2+ ions and reactive red 120 azo dye (RR-120).22 A MgAl–LDH/HNT composite showed a highly efficient CO2 adsorption performance with an adsorption capacity of 3.91 mmol g−1.23 Thus, HNTs could be a potential and ideal material to construct functional mineral composites for removing water pollutants.24,25
Recently, SnS2 has received increasing attention in water treatment due to its good adsorption performance, stable chemical properties, and simple synthesis.26–28 SnS2 nanoparticles exhibited an adsorption efficiency of 85% toward rhodamine B within 180 min.29 Compared to SnS2 with other morphologies, layered SnS2 could remove a large number of toxic organic dyes by selective adsorption, which further highlighted its advantages in pollutant removal.30 Moreover, the layered structure could effectively improve the diffusion of dye molecules, provide better transport paths, and offer a large number of adsorption sites for the adsorption process.
It was reported that the carbon modification of HNTs could bring about an expansion of the specific surface area and an increase in the number of adsorption sites, which further improved the adsorption efficiency.31 Thus, it is anticipated that composites constructed using HNTs with carbon modification and layered SnS2 could be ideal and potential adsorbents for removing water pollutants.32,33
In this work, HNTs modified with EDTA after calcination were used as supports for loading layered SnS2 to construct SnS2/HNTs(C) (SHCx-y) composites. The synthesized adsorbents possessed large specific surface areas, rich porous structure, and more negative surface charge, making them suitable for MB removal. The adsorption conditions including MB concentration, adsorbent dosage, temperature, and pH value were systematically optimized. The important role of carbon modification of HNTs in enhancing the removal efficiency was emphatically discussed. Moreover, the adsorption process of MB over SHC0.04-500 was examined and a plausible adsorption mechanism was put forward.
![]() | (1) |
![]() | (2) |
In order to investigate the wide applicability of the adsorbent, various organic dyes (MV, OA, and MO) and antibiotics (OFX, NFO, and TC) were selected to conduct adsorption tests. The concentrations of the above pollutant solutions were all 50 mg L−1.
Fig. 2a shows the TEM image of SHC0.04-500. It could be clearly observed that SnS2 nanosheets were uniformly anchored on the surface of HNTs(C)-500, demonstrating the successful synthesis of SHC0.04-500. The red area in the HRTEM image signifies the amorphous graphite carbon, indicating the anticipated carbon modification of HNTs (Fig. 2b). Additionally, the lattice spacing of 0.27 nm was indexed to the (101) crystal plane of SnS2, verifying the well-crystallized structure of SnS2 in the composite. In Fig. 2c, carbon was found to be uniformly distributed across the entire structure, further confirming the successful carbon modification of HNTs. Notably, Al and Si elements were detected in the tubular regions, while Sn and S elements were concentrated in the hexagonal lamellar domains. This spatially correlated elemental distribution provided direct evidence for the intimate integration of HNTs(C)-500 and SnS2, further confirming the successful synthesis of the SHC0.04-500 composite.
To further elucidate the detailed structural information and compositions of all samples, XRD and FT-IR techniques were adopted. The XRD patterns of HNTs and pure SnS2 matched well with the standard PDF cards of HNTs and SnS2 (JCPDS No. 09-0453 and JCPDS No. 23-0677), respectively (Fig. 3a). The characteristic peaks located at 15.0°, 32.1°, and 41.9° correspond to the (001), (101), and (102) crystal planes of SnS2, respectively. The broad peak at 24° in the XRD pattern of HNTs(C)-500 indicates the presence of amorphous carbon.34,35 The carbon layer might make it difficult to detect the characteristic peaks of HNTs.36 Therefore, SHC0.04-500 obviously showed the diffraction peaks of SnS2, and the intensity of the SnS2 diffraction peaks increased with a decrease in the addition amount of HNTs(C)-500 (Fig. S1†).
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Fig. 3 XRD patterns (a), FT-IR spectra (b), Raman spectra (c), and N2 adsorption–desorption isotherms (d) of various samples. |
The FT-IR spectra of the pure and composite samples are shown in Fig. 3b. The absorption peaks at 542 and 912 cm−1 in HNTs belong to the bending vibration of Al–O–Si and the deformation vibration of Al–OH, respectively.37 The absorption peaks at 1022 and 1107 cm−1 correspond to the stretching vibrations of Si–O–Si and Si–O bonds in HNTs, respectively. In the spectrum of SnS2, the characteristic peak at 1402 cm−1 was attributed to the vibration of Sn–S bonds.38 For SnS2 and HNTs, the absorption peaks at 3618 and 3693 cm−1 were attributed to the stretching vibrations of the hydroxyl groups on the surfaces of SnS2 and HNTs, respectively.16 Notably, the two broad peaks near 1100 and 3600 cm−1 disappeared after HNT modification, indicating that the hydroxyl groups were removed from the surfaces of HNTs after high-temperature calcination.39 All samples showed the peak at 1630 cm−1, which was attributed to the adsorbed water molecules. It was noteworthy that the peak at around 1000 cm−1 in SHC0.04-500 shifted compared with that in pure HNTs(C)-500, which might be caused by the formation of new Si–O–Sn bonds.40 The above phenomenon proved the successful combination of SnS2 with HNTs(C)-500.41 The intensity of the peak at 1402 cm−1 in SHC0.04-500 increased in contrast to that of SnS2, which might be due to that there was a strong interaction between the C–C bond in HNTs(C)-500 with the Sn–S bond in SnS2.40
Raman spectrometry was employed to confirm the graphitization of various samples (Fig. 3c). There were two significant bands at 1385 and 1590 cm−1 in SHC0.04-500 and HNTs(C)-500, which imply the point defect degree (D band) and the graphitic structures (G band), respectively. The intensity ratio of the D band to the G band (ID/IG) is generally used to describe the degree of graphitization of samples. The larger the ratio, the greater the degree of graphitization, i.e., more defects were produced. According to the Raman results, the ID/IG value of SHC0.04-500 (0.88) was significantly higher than that of SnS2/HNTs (0), suggesting that the modification of HNTs with EDTA and subsequent calcination positively affected the graphitization of SHC0.04-500.42 The D and G bands were not observed in pure SnS2 and HNTs.
Fig. 3d shows the N2 adsorption–desorption isotherms of various samples. All the prepared samples exhibited type IV isotherms. SHC0.04-500 had an obvious hysteresis loop, which was characteristic of a mesoporous structure. The SHC0.04-500 sample exhibited the largest specific surface area (118.49 m2 g−1), which was larger than those of SnS2 (30.90 m2 g−1), HNTs (40.09 m2 g−1), and HNTs(C)-500 (52.24 m2 g−1). The larger specific surface area of SHC0.04-500 endowed it with more adsorption sites, which was favorable for enhancing the adsorption efficiency of SHC0.04-500.
Fig. 4 shows the survey XPS spectra of SnS2, HNTs, HNTs(C)-500, and SHC0.04-500 as well as the high-resolution XPS spectra of each element. Fig. 4a shows that Sn, S, O, Si, Al, and C elements were all present in the SHC0.04-500 sample. The high-resolution C 1s spectra are shown in Fig. 4b. The characteristic peaks appearing at 288.9, 286.5, and 284.8 eV were attributed to the O–CO, C–O, and C–C bonds, respectively. The peak area of sp2 hybridized carbon (284.8 eV) increased from 60.48% (HNTs) to 73.64% (HNTs(C)-500), indicating that modification of HNTs with EDTA was beneficial for increasing the graphitic carbon content, which was consistent with the results of Raman analysis.43 The content of C–C in SHC0.04-500 was 70.6%, which was slightly smaller than that of C–C in HNTs(C)-500. This phenomenon suggested that some of C–C bonds in HNTs(C)-500 were broken and reorganized due to the interaction between SnS2 and HNTs(C)-500 during the synthesis process.44
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Fig. 4 Survey XPS spectra (a) and high-resolution spectra of C 1s (b), Sn 3d (c), S 2p (d), Al 2p (e), and Si 2p (f) of various samples. |
As shown in Fig. 4c, Sn 3d spectra exhibited two binding energies at 494.8 and 486.4 eV, belonging to Sn 3d1/2 and Sn 3d3/2, respectively. In comparison with pure SnS2, the fitted peak of Sn 3d in SHC0.04-500 shifted to a lower-binding-energy position. In Fig. 4d, the characteristic peaks attributed to S 2p3/2 and S 2p1/2 orbitals shifted from 163.1 and 161.8 eV in SnS2 to 162.5 and 161.3 eV in SHC0.04-500, respectively, which suggested that the presence of HNTs(C)-500 had an effect on the electronic state of SnS2.45,46
Fig. 4e and f separately show the characteristic peaks of Al 2p and Si 2p. For HNTs, both Al–O–Al and Si–O–Si bonds showed only one characteristic peak at 74.3 and 102.4 eV, respectively. In comparison with HNTs, the peak positions of Al 2p and Si 2p in SHC0.04-500 shifted to a lower binding-energy position. It was noteworthy that the binding energies of Sn 3d, S 2p, Al 2p, and Si 2p in SHC0.04-500 were all lower than those of pure SnS2 and HNTs(C)-500. This phenomenon not only confirmed the successful preparation of SHC0.04-500 but also provided direct evidence that SnS2 and HNTs(C)-500 were not merely physically mixed. Instead, their intrinsic electronic environments had been modified through interfacial interactions, which altered the electron distribution around these elements and thereby resulted in the observed decrease in binding energy.47
MB was selected as the target pollutant to investigate the removal performance of various samples. The SnS2, HNTs, and HNTs(C)-500 samples could adsorb a small amount of MB with adsorption efficiencies of only 10.5%, 9.1%, and 5.0% within 18 min, respectively (Fig. 5a). The adsorption efficiency of SHC0.04-500 was significantly improved, showing about 90% adsorption efficiency toward MB within 18 min, which was about 9, 10, and 18 times as those of SnS2, HNTs, and HNTs(C)-500, respectively.
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Fig. 5 The adsorption efficiencies of various samples (a), HNTs(C) at different calcination temperatures (b), and HNTs(C)-500 with different dosages toward MB (c). |
For exploring the optimal calcination temperature of modified HNTs, adsorption tests of MB over a series of SHC0.5-y samples were performed. As shown in Fig. 5b, it could be observed that the adsorption efficiencies of the composites increased first and then decreased with increasing the calcination temperature of HNTs(C). At a lower temperature of 400 °C, the graphitization of the HNTs(C)-400 was low, which was not favorable for adsorption. When the calcination temperature reached 500 °C, the carbon in HNTs(C) formed a more regular graphite structure, resulting in a stronger interaction between the carbon layer and MB molecules, which could significantly improve the adsorption capacity.48 However, with further increasing the temperature, the adsorption sites decreased due to the oxidation of the carbon layer on HNTs.49 Based on the above analysis, 500 °C was adopted as the optimal calcination temperature in the following experiments.
Fig. 5c shows the effect of HNTs(C)-500 dosage on the adsorption efficiency of SHCx-500. The adsorption efficiency increased first and then decreased with an increase of HNTs(C)-500 dosage. Based on the economic consideration, 0.04 g was selected as the optimal HNTs(C)-500 dosage in the subsequent experiments.
Fig. 6a shows the influence of MB concentration on the adsorption performance of SHC0.04-500. The adsorption efficiency could reach more than 90% within 18 min, which decreased gradually with further increasing the initial MB concentration. The decreased adsorption efficiency indicated the insufficient active sites of SHC0.04-500 for the enhanced number of MB molecules. Therefore, the initial MB concentration of 50 mg L−1 was chosen for the next experiments. Fig. 6b shows the effect of SHC0.04-500 dosage (5, 10, 15, 20, 25, and 30 mg) on the removal efficiency of MB. The adsorption efficiency increased obviously with an increase of SHC0.04-500 dosage and reached 100% when the SHC0.04-500 dosage was enhanced to 25 mg, which remain unchanged with further increasing the adsorbent dosage to 30 mg. This phenomenon might be explained by the increased number of active sites with increasing adsorbent dosage, leading to an increased adsorption efficiency.
In order to investigate the effect of temperature on the adsorption efficiency, adsorption experiments were carried out at different temperatures (0, 20, 40, and 60 °C) (Fig. 6c). It could be found that the temperature had no remarkable effect on the removal efficiency, just accelerated the adsorption rate of SHC0.04-500 toward MB. From the point view of energy saving, 20 °C was selected as the optimal temperature for adsorption over SHC0.04-500. Based on the above results, it could be deduced that the adsorbent SHC0.04-500 had a promising application at variable temperatures.
The adaptability of an adsorbent in a wide pH range is very important for the practical application of the adsorbent. Fig. 6d shows the influence of pH value on the removal performance of SHC0.04-500 toward MB. The adsorption efficiency reached 15% when the pH value was 3. As the pH value continued to rise, the adsorption efficiency showed a remarkable increase, which achieved the highest efficiency at pH = 11. This result demonstrated the adaptability of SHC0.04-500 under conditions close to neutral and alkaline
For investigating the applicability of SHC0.04-500 to other dyes, adsorption experiments were carried out through selecting four different dyes as target pollutants (Fig. 6e). The cationic dyes MV and MG could be adsorbed over 85% to SHC0.04-500. In contrast, the adsorbent showed very low adsorption efficiencies toward the anionic dyes OA and MO. Fig. 6f shows the zeta potential plots of SHC0.04-500 at different pH values. When the pH value was 3, the surface of the adsorbent was positively charged, resulting in a lower adsorption efficiency toward MB. In contrast, when the pH value was increased from 3 to 11, the surface was negatively charged, leading to a higher adsorption efficiency toward MB. It was obvious that the adsorbent showed the excellent adsorption performance toward cationic dyes, thus it could be deduced that the electrostatic attraction was possibly the key factor in the adsorption process.
The adsorption efficiencies of SHC0.04-500 toward various antibiotics with a concentration of 50 mg L−1 were also examined (Fig. S2†). SHC0.04-500 showed the highest adsorption efficiency toward NFO, which was close to 80% within 18 min. The results indicated that SHC0.04-500 had great potential in removing antibiotics from wastewater.
The results of the cyclic adsorption experiments of MB over SHC0.04-500 are shown in Fig. 7a. The adsorption efficiency decreased by only 5% after the first cycle, which still remained 78% after the fourth cycle. The decreased adsorption efficiency was probably related to the incomplete desorption and adsorbent loss.50 After the adsorption of MB, the color of the adsorbent changed from yellow to dark green, and the dark blue MB turned to light blue, suggesting that MB was successfully adsorbed by SHC0.04-500 (Fig. 7b).51
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Fig. 7 The cycling performance of SHC0.04-500 (a). The color images of SHC0.04-500 and MB (b). XRD patterns (c) and FT-IR spectra (d) of SHC0.04-500 before and after adsorption. |
Fig. 7c demonstrates that the XRD pattern of SHC0.04-500 basically remains unchanged after the adsorption. A new peak at 1327 cm−1 emerged in the FT-IR spectra of SHC0.04-500 after the adsorption, which was attributed to the C–C stretching vibrations of MB.52 Moreover, two spurious peaks at 1244 and 1490 cm−1 related to the C–N stretching vibration of N–CH3 in the MB structure were also detected in SHC0.04-500 after adsorption, implying the successful adsorption of MB molecules on the surface of SHC0.04-500.53 Based on the above analysis, it could be concluded that SHC0.04-500 exhibited excellent cycling and structural stability during the cycle tests.
Pseudo-first-order and pseudo-second-order models were employed to describe the adsorption process of SHC0.04-500 toward MB. The pseudo-first-order and pseudo-second-order equations are presented as formulas (3) and (4), respectively:54
ln (qe − qt) = ln![]() | (3) |
![]() | (4) |
According to Fig. 8a, b, and Table S1,† the adsorption process of SHC0.04-500 toward MB had both physical and chemical adsorption. The adsorption data matched well with the pseudo-first-order model (R2 = 0.99621) than the pseudo-second-order model (R2 = 0.99325), implying that the physical adsorption played a dominant role in MB adsorption over SHC0.04-500.
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Fig. 8 The pseudo-first-order model (a) and the pseudo-second-order model (b) for MB adsorption over SHC0.04-500. |
From the above Raman results, it could be seen that SHC0.04-500 and HNTs(C)-500 had obvious G bands compared with HNTs, indicating that SHC0.04-500 and HNTs(C)-500 contained a large number of aromatic structures with π electron clouds. Due to the conjugated π bond structure of MB, it was attracted to SHC0.04-500 through π–π stacking, causing their electron clouds to overlap and resulting in chemical adsorption. The results showed that carbonized HNTs played a certain role in promoting chemical adsorption.
The adsorption isotherm models are proposed to explain the adsorption equilibrium and express the interactions between adsorbent and adsorbed molecules.55 In this study, four adsorption models were used to analyze the adsorption data, including Langmuir, Temkin, Redlich–Peterson, and Freundlich models. The specific model expressions are shown in eqn (5)–(8), respectively.
![]() | (5) |
qe = A![]() | (6) |
![]() | (7) |
![]() | (8) |
The fitting results of the four adsorption isotherm models are shown in Fig. 9 and Table S2.† The fitting coefficient of the Langmuir isotherm model (R2 = 0.96934) was higher than those of the Freundlich (R2 = 0.91509), Temkin (R2 = 0.95782), and Redlich–Peterson (R2 = 0.96034) isotherm models, suggesting that the Langmuir isotherm model could better describe the equilibrium data. The Langmuir model is based on the assumption of monolayer adsorption on the surface of a homogeneous adsorbent, where all adsorption sites are identical and there is no interaction between the adsorbed molecules.56 Therefore, the adsorption of MB over SHC0.04-500 was monolayer adsorption.
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Fig. 9 Langmuir (a), Temkin (b), Redlich–Peterson (c), and Freundlich (d) isothermal models for MB adsorption over SHC0.04-500. |
As shown in Fig. S3,† HNTs(C)-500 exhibited a higher surface charge density than pristine HNTs, indicating that the carbon layer introduced the additional negative charges on the surface of HNTs(C)-500. In combination with the intrinsic charge properties of SnS2, the electrostatic attraction toward the cationic dye MB was undoubtedly enhanced. Notably, at pH >3, all samples (HNTs, SnS2, HNTs(C)-500, and SHC0.04-500) have negative charges and SHC0.04-500 exhibited the highest value. This enhancement was possibly related to the covalent bond formation between SnS2 and HNTs(C)-500 during the composite synthesis, which induced electron redistribution and thus increased the overall negativity of SHC0.04-500. Therefore, SHC0.04-500 exhibited significantly higher adsorption efficiency toward cationic dyes than anionic dyes, which was consistent with the principle of opposite charge attraction. The kinetic and isotherm models revealed that the adsorption process conformed to the typical physical adsorption. The zeta potential data confirmed a strong relationship between the enhanced surface negativity of SHC0.04-500 and its superior MB adsorption performance. It can be concluded that the electrostatic attraction dominated the adsorption process of MB over SHC0.04-500.
Fig. S4 and Table S3† show the pore size distribution curves, surface areas, and pore size distribution data of various samples, respectively. HNTs(C)-500 had a larger specific surface area than HNTs, which suggested that the carbon layer on HNTs was beneficial for increasing the specific surface area. SHC0.04-500 had the largest specific surface area in comparison with those of HNTs, HNTs(C)-500, and SnS2. The larger specific surface area and smaller mesopores could provide more active sites, which was beneficial for enhancing the adsorption performance. The specific surface area and pore size of SHC0.04-500 changed after MB adsorption (Fig. S5 and Table S3†), although the changes were not significant. This indicates that only a small portion of MB molecules had attached to the surface and filled the pores of SHC0.04-500. Based on the above analysis, the large specific surface area and pore filling also contributed to the enhanced adsorption efficiency of SHC0.04-500 toward MB.
Moreover, the results of FT-IR spectroscopy suggested that a new peak at 887 cm−1 emerged in the FT-IR spectrum of HNTs(C)-500. This new peak was attributed to the C–H bond, which could provide active sites for adsorption. The peak intensity of SHC0.04-500 at 887 cm−1 increased after MB adsorption, indicating that the C–H bending vibration was affected. Thus, it could be deduced that there was a π–π interaction between SHC0.04-500 and MB molecules, which was possibly another factor promoting the adsorption process.57
In summary, there were four main factors contributing to the enhanced adsorption performance of SHC0.04-500 toward MB, including electrostatic attraction, pore filling, large specific surface area, and π–π interactions (Fig. 10).
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d5dt01400j |
This journal is © The Royal Society of Chemistry 2025 |