Thorium, as an important radioactive element, is widely present in nature, and its accompanying environmental pollution is also serious. Extracellular polymeric substances (EPS) are commonly found on the surface of microbial bodies and have strong adsorption capacity for metal ions. In this study, four methods were used to extract EPS from indigenous bacteria of rare earth tailings and to determine the best extraction method. The extracted EPS was applied to treat Th4+, and the changes in functional groups and composition of EPS were investigated. The results showed that the ultrasonic method was more efficient than other methods. The best removal efficiency was observed at pH 3.5, Th4+ concentration of 20 mg/L, and EPS dosage of 30 mL at 25 °C. After 9 h, the adsorption process reached equilibrium with a maximum removal efficiency of 75.93% and a maximum theoretical adsorption capacity of 25.96 mg/g. The Th4+ removal process was consistent with the Langmuir and Freundlich adsorption isotherms and the kinetic data were consistent with the pseudo-second-order kinetic model, which is mainly based on chemisorption. Amide I and amide II of proteins, C–H from aliphatic, as well as O–H and C = O from carboxylic acid play important roles in the adsorption process.

  • EPS are extracted from indigenous bacteria of rare earth tailings and it has better polysaccharide content than other EPS extracted from other materials.

  • Application of EPS to the treatment of Th4+ exhibited better adsorption effects.

  • The functional groups of EPS play important role in the adsorption of Th4+.

Graphical Abstract

Graphical Abstract
Graphical Abstract

Thorium, as a radionuclide, mainly exists in thorium ore, uranium ore and rare earth minerals. In nature, thorium occurs mainly in the form of tetravalent compounds (Th4+). The Bayan Obo rare earth mine in Baotou has the largest thorium content in China, accounting for 77.3% of the total thorium reserves in China (Xu et al. 2005; Chen et al. 2022). Nowadays, Baotou Bayan Obo rare earth mine has been widely used in energy conservation, environmental protection, green industry, and other low-carbon economic fields. With the popularity of concepts including clean energy, and carbon neutrality, the demand for high-property rare-earth permanent magnetic materials is growing rapidly. The rare-earth permeability is likely to continue to increase.

While rare-earth is fully and efficiently utilized, thorium is not utilized due to its low industrial value, and is often discharged in the form of thorium wastewater, loss, and flying, which not only causes serious pollution to the soil environment around the mining area, but also greatly threatens the safety of groundwater (Xu et al. 2005; Chen et al. 2022). Thorium is not biodegradable and it tends to accumulate in the human body, causing serious damage (Cadena 1983; Yang et al. 2017). Currently, common treatment methods for thorium containing wastewater include adsorption, ion exchange, membrane technologies, solvent extraction, and chemical precipitation (Li et al. 2018). Traditional chemical and physical treatment methods have disadvantages such as high cost, complicated operation, and unstable effects. However, adsorption is a simple technique that does not require any special set up and the originality resides in the material itself (Hamane et al. 2015). Biosorbents are safe and less polluting to the environment. This is a new heavy metal treatment method that has been proven to have the most potential for development by previous research.

Extracellular polymeric substances (EPS), as a new kind of biological adsorbent, have been widely studied because of their unique advantages in heavy metal adsorption. EPS are high-molecular-weight mixtures that mainly consist of polysaccharides, proteins, humus, fat, nucleic acid, and inorganic substances (Li et al. 2018). It is produced, excreted, secreted, and absorbed by cells (mainly bacteria). EPS binds closely with cells and only be extracted by special physical or chemical methods.

In recent years, EPS have been widely applied in various fields such as wastewater treatment, cosmetic industries food, and pharmaceuticals due to their physicochemical and biological properties (Xiao & Zheng 2016). Some studies have shown that EPS extracted from different sources can effectively remove heavy metals (More et al. 2014; Nouha et al. 2016; Zhao et al. 2016). However, the raw materials used to extract EPS in the past are usually only for sludge and bacteria (Wang et al. 2014; Gupta & Batul 2016; Wei et al. 2016), while the extraction of EPS from indigenous bacteria of rare earth tailings and further treatment of thorium containing wastewater is relatively little investigated. In this study, indigenous bacteria of rare earth tailings were used to extract EPS and it was applied to the treatment of Th4+, and the optimal extraction method, content, and interaction mechanism of EPS with Th4+ were explored.

Experimental reagent

Anthrone, EDTA, and Coomassie Blue (G-250) were from Sinopharm Chemical Reagent Co., Ltd., HCl from Nanjing Chemical Reagent Co., Ltd., H2C2O4 from Fuchen (Tianjin) Chemical Reagent Co., Ltd., C22H18As2N4O14S2 and NaOH from Tianjin Chemical Reagent Factory I. H2SO4 was from the Beijing Chemical Plant. Bovine serum albumin (BSA) from Tianguangyuan (Xian) Biotechnology Co., Ltd., Glucose from Xilong Scientific Co., Ltd., and Th(NO3)4·4H2O was supplied by the Beijing Research Institute of Chemical Metallurgy of China National Nuclear Industry Co.. The reagents used in the experiments were analytically pure. All the solutions in the experiment were made from deionized water.

Tailings samples

Tailings collected from the rare earth tailings dam in Baotou city, Inner Mongolia autonomous region, China were used in this study. The tailings are washed with water, dried, crushed, and sieved. Of these, tailings with an average diameter of less than 2 mm were used for the following studies.

Microbial strains

Rare earth tailings samples were used as the source of strains, and the target strains were screened by the diluted plate method. The 1 g of tailings sample was transferred to a conical flask containing 99 mL of sterile saline water and shaken to make a suspension, which was allowed to stand for 1 min. The suspension was diluted in a 10-fold gradient, inoculated on LB solid medium and cultivated for 1–2 d at 32 °C in a constant temperature incubator (Han et al. 2020). The most numerous individual colonies on the medium with regular edges and smooth upper surfaces and larger diameters (about 3 mm) were selected and streaked repeatedly on the same solid medium for separation. The target strains were obtained when the colony morphology was consistent on the medium. A bacterial strain, named K-1, was isolated and screened from the tailings sample, and the strain K-1 was sent to Shanghai Meiji Biomedical Technology Co., Ltd for 16S rDNA sequence analysis (Han et al. 2020). The ITS sequence was compared with BLAST sequence similarity in the NCBI online database, and it was found that strain K-1 and Lysinibacillus sp. strain LJ75 were located in the same branch with 100% similarity, so strain K-1 was identified as Lysinibacillus fusiformis.

Extraction methods of EPS

In this study, the comparison experiments involved four conventional extraction methods, including, ultrasound, heating, and treatment with NaOH and EDTA. The isolated individual strain K-1 was inoculated into LB liquid medium and proliferated at a constant temperature of 32 °C for 24 h, which was the sample bacteria liquid for EPS extraction. Specific extraction procedures are described in Figure 1.
Figure 1

Four EPS extraction processes.

Figure 1

Four EPS extraction processes.

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All the EPS samples were measured immediately to avoid the degradation of EPS during storage. After the extraction, the protein and polysaccharide were quantified, and the concentration of EPS was used to express the sum of the two contents. The concentration of EPS was used to perform unit conversions (Kang et al. 2016).

EPS analysis

The functional groups of EPS were also analyzed by Fourier Transform Infrared spectrometer (FTIR) (BRUKER TensorII, Germany) with a resolution of 4 cm−1 and scan a range of 400–4000 cm−1. EPS was freeze dried by a lyophilizer (Alpha 1-2 LDplus, Christ, Germany) before FTIR determination. The EPS before and after adsorption was added to a 1 cm quartz cuvette and placed in the 3D-EEM (HITACHIF4600, Hitachi Limited, Tokyo, Japan) to determine its composition changes. The scanning interval was 5 nm, while the scanning speed was 12,000 nm/min. The infrared and fluorescence spectrum were analyzed by Origin 2018.

The protein contents were determined using the Coomassie Blue method, with bovine serum albumin (BSA) as the standard. The polysaccharide contents were measured using the anthrone-sulfuric acid method, with glucose as the standard.

Th4+ adsorption experiments

The experiments were conducted in 250 mL conical flasks containing 20 mL of Th4+ solution at 25 °C. The 30 mL of EPS extracted by different methods were used as adsorbent and placed in dialysis bags and then in conical flasks. The conical flasks were agitated at 150 r/min on a thermostatic oscillator for 15 h, allowing ample time for adsorption equilibrium. To determine the biosorption isotherms, the initial Th4+ concentration was varied from 10 to 50 mg/L while the EPS dosage in each experiment was held constant at 30 mL. After 15 h, 1 mL of the solution in the conical flask was taken and added to the 10 mL colorimetric tube and 1 mL of 10% oxalic acid solution was added to the colorimetric tube and shaken well. Then 0.5 mL of 0.05% Arsenazo iii solution was added as the chromogenic agent and finally titrated to the scale line with 7 mol/L HCl, shook well, and stood for 10 min. The residual metal ion concentration (Ce) in the solution was determined by UV-visible spectrophotometer (752N, Shanghai Yidian Analytical Instruments Co., Ltd, China) at 660 nm. The removal efficiency R (%) and adsorption capacities qe (mg/g) of Th4+ by EPS were calculated based on the concentration difference before and after the reaction, as shown in Equations (1) and (2):
(1)
(2)
where C0 and Ce (mg/L) are the initial and equilibrium Th4+ concentrations, respectively; V is the volume of the solution, L; m is adsorbent dosage, g.

Comparison of extraction methods of EPS

FTIR spectra of EPS extracted by different methods

FTIR spectra examples of EPS extracted from different methods are presented in Figures 2 and 3. Table 1 recaps the functional groups corresponding to bands observed on FTIR spectra of EPS extracted by different methods. The different functional groups observed in the EPS samples extracted by indigenous bacteria of rare earth tailings are similar to Tang's results (Tang et al. 2021).
Table 1

Main functional groups observed from FTIR spectra of EPS

WavenumberVibration type and corresponding functional groups
3200–3420 Stretching vibration of O–H groups of carbohydrates and N–H groups of proteins 
2900–3000 Stretching vibration of methyl and methylene C–H 
1625–1660 Stretching vibration of C = O and C–N (amide I) of proteins 
1592 Stretching vibration of C–N and deformation vibration of N–H (amide II) of Proteins (peptidic bond) 
1380–1460 Aliphatic C–H bending vibration and stretching vibration of C = O in carboxylates 
1235–1245 Stretching vibration of O–H and deformation vibration of C = O of carboxylic acid 
1040–1080 Stretching vibrations of C–O–O and C–O, which may be caused by carbohydrate sand aromatics 
<1000 Fingerprint region presented the existence of phosphate or sulfur functional groups 
WavenumberVibration type and corresponding functional groups
3200–3420 Stretching vibration of O–H groups of carbohydrates and N–H groups of proteins 
2900–3000 Stretching vibration of methyl and methylene C–H 
1625–1660 Stretching vibration of C = O and C–N (amide I) of proteins 
1592 Stretching vibration of C–N and deformation vibration of N–H (amide II) of Proteins (peptidic bond) 
1380–1460 Aliphatic C–H bending vibration and stretching vibration of C = O in carboxylates 
1235–1245 Stretching vibration of O–H and deformation vibration of C = O of carboxylic acid 
1040–1080 Stretching vibrations of C–O–O and C–O, which may be caused by carbohydrate sand aromatics 
<1000 Fingerprint region presented the existence of phosphate or sulfur functional groups 
Figure 2

FTIR spectra of EPS extracted by physical methods.

Figure 2

FTIR spectra of EPS extracted by physical methods.

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Figure 3

FTIR spectra of EPS extracted by chemical methods.

Figure 3

FTIR spectra of EPS extracted by chemical methods.

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For EPS extracted by ultrasonic and heating, the same characteristic bands can be observed on every EPS FTIR spectra presented in Figure 2. Bands 3200–1592 cm−1 can be attributed to protein and polysaccharide functional groups. Carboxylic groups, under acid or basic salt form, are responsible for some less intense bands and they suggest, when combined with the other observed bands, the presence of uronic acids and of humic substances (Comte et al. 2006). The band at 2347 cm−1 of EPS FTIR spectrum extracted by the heating method may be caused by sample contamination in the testing process.

The FTIR spectra of EPS extracted by chemical methods (Figure 3) show particular bands which do not appear for EPS extracted by the physical methods. For the FTIR spectrum obtained for EPS extracted by the treatment with EDTA, the bands 1332 and 1240 cm−1 are seen to be associated with C–N stretching. Moreover, bands 1592 cm−1 are attributed to carboxylate functions. This demonstrates contamination of EPS by the chemical reagent. This is consistent with previous experimental results. The FTIR spectrum obtained for EPS extracted by the NaOH method shows a band at 2345 cm−1. These bands could be interpreted as specific bands for the result of a NaOH and EPS reaction (Comte et al. 2006).

Effects of different extraction methods on EPS content

EPS of the indigenous bacteria of rare earth tailings were extracted following the procedures in section 2.4. The quantities of proteins and polysaccharides were measured to represent the EPS yields, as they are the main component of EPS. The experimental results are shown in Table 2. The results show that the content of polysaccharides in EPS extracted from the indigenous bacteria of rare earth tailings was higher than that of protein. This is similar to the research results of Zhang et al. (2008). The results indicated that the yields of EPS were highly dependent on the extraction method. The content of total EPS and protein extracted by the ultrasonic method is the highest among the four extracted methods indicating that ultrasonic method is the best method to extract this sample EPS. Thus, all EPS extracted by the ultrasonic method was applied in the subsequent experiments.

Table 2

The total amount of EPS and the content of each component using different extraction methods

Extraction methodTotal EPS (mg/L)Protein (mg/L)Polysaccharide(mg/L)
Ultrasonic 68.95 14.50 54.45 
Heating 68.77 14.02 54.75 
EDTA 57.65 12.51 45.14 
NaOH 62.61 12.44 50.17 
Extraction methodTotal EPS (mg/L)Protein (mg/L)Polysaccharide(mg/L)
Ultrasonic 68.95 14.50 54.45 
Heating 68.77 14.02 54.75 
EDTA 57.65 12.51 45.14 
NaOH 62.61 12.44 50.17 

As shown in Table 2, the contents of polysaccharides of EPS extracted by ultrasonic method are the highest. This is because the ultrasonic method uses ultrasonic shear force, cavitation, and so on to make EPS off the cell surface into the water. The action intensity is mild, which can effectively separate the effective components of EPS at the same time, but can avoid damaging the effective components of EPS. The content of polysaccharides extracted by heating method was the highest among the four methods. Increasing the temperature will lose the structure of the sample and could decrease van der Waals forces and hydrogen bonding between EPS and cells (Li & Yang 2007; Guo et al. 2010; Zhou et al. 2016), and extract the firmly bound EPS while the proteins and polysaccharides in EPS can be hydrolyzed in the extraction process. In Table 2, the biochemical composition content was lower in the EPS extracted by treatment with NaOH than in other methods. The addition of NaOH solution caused the groups, such as carboxylic groups, to be ionized, resulting in a strong repulsion and then separation between the EPS and the cells, which lysed the cells and increased the possibility of cell rupture (Huang et al. 2021). The EDTA method had the lowest polysaccharide content, and the protein content was only 0.07 mg/L higher than the NaOH method. Liu & Fang (2002) suggested that there was formation of complexes between EDTA and the EPS. These EDTA-EPS complexes were not removed by membrane separation and thus the EDTA remained in the EPS. Chemical extraction EPS will be contaminated by chemical reagents which may affect the determination of EPS components.

In the subsequent experiments, EPS was extracted by ultrasonic method. The EPS concentration was 68.95 mg/L, which was used as the basis for the EPS dosage in the adsorption test.

Mechanism of EPS adsorption Th4+

FTIR spectra analysis

The functional groups in EPS are a significant factor that influences Th4+ adsorption (Tang et al. 2021). The FTIR spectra of EPS before and after Th4+ adsorption is illustrated in Figure 4. From an overall perspective, the profiles of FTIR spectra for the EPS before and after Th4+ adsorption were similar, suggesting that their chemical groups are similar. However, some differences in the peaks can be found after careful comparison of the FTIR spectra. Firstly, the EPS showed the changes after Th4+ adsorption, that is, the peak at 3279 cm−1 changed, implying a possible interaction between Th4+ and C–H from methyl and methylene. Secondly, for EPS, the respective intensity of the peaks at about 1631 and 1532 cm−1 was found to decrease after Th4+ adsorption. This indicated that amide I and amide II of proteins played a crucial role during Th4+ adsorption. Additionally, the bands ranging from 1387 to 1227 cm−1 changed irregularly after Th4+ bonding. This implied that those aliphatic C–H stretching vibration and O–H and C = O related carboxylic acid also made a great contribution to Th4+ adsorption. Combining with the variations in functional groups of EPS extracted by ultrasonic method from tailing observed above, it was deduced that amide I and amide II of proteins, C–H from aliphatic, as well as O–H and C–O from carboxylic acid, play the significant role in Th4+ adsorption. These functional groups in EPS could coordinate with Th4+ to form chelates, thereby removing Th4+ in aqueous solution (Tang et al. 2021).
Figure 4

FTIR spectra before and after Th4+ adsorption.

Figure 4

FTIR spectra before and after Th4+ adsorption.

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3D-EEM analysis

The fluorescence changes of EPS before and after adsorption are shown in Figure 5. It can be seen from Figure 5 that peak A and peak D are tryptophan-like fluorescent substances located at Ex/Em = 280/325 nm, Ex/Em = 285/345 nm while peak B is a tyrosine-like fluorescent substance located at Ex/Em = 230/320 nm. Both of them are fluorescent proteins, because of the aromatic cyclic amino acids in EPS (Guo et al. 2014). Peak C is a humic acid-like substance located at Ex/Em = 337/416 nm. The results of the study showed that the extracted EPS mainly consisted of tryptophan and tyrosine-based proteins. Since tryptophan and tyrosine are hydrophobic amino acids with strong hydrophobic side chains that provide hydrophobic adsorption sites mainly on EPS, this allows Th4+ to bind tightly to EPS. Previously published studies have shown that the fluorescence intensity is closely related to the content of EPS (Ma et al. 2018). It can be seen from the figure that the fluorescence intensity of tryptophan after adsorption was significantly weakened and the EPS content was reduced. The above results indicate that protein is the main component of EPS and plays an important role in the adsorption process. In addition, some humus-like substances have increased slightly.
Figure 5

3D-EEM before (a) and after (b) Th4+ adsorption.

Figure 5

3D-EEM before (a) and after (b) Th4+ adsorption.

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Effect of pH on adsorption of Th4+ by EPS

The pH value is one of the most significant environmental factors influencing not only site dissociation, but also the speciation and the biosorption availability of heavy metals (Özer et al. 2004). The variation of removal efficiency and adsorption capacities with the pH is shown in Figure 6. The adsorption increases with increasing pH and reaches a maximum (R = 78.01%; qe = 26.6926 mg/g) at pH = 3.5. At pH < 3.5, the surface of EPS would be surrounded by H3O+ ions which compete with Th4+ for the adsorption sites and decrease the Th4+ interaction with binding sites of the surface of EPS by greater repulsive forces (Özer et al. 2004). As pH increases, the acidity of the solution decreases while the number of binding sites increases, and therefore, the adsorption of Th4+ increases. At pH>3.5, the metal ions combine with various anions in the solution to form negatively charged groups, which are not easy to combine with the adsorption site. The results showed that the optimal pH for Th4+ to be adsorbed was 3.5.
Figure 6

Effect of different pH on Th4+ removal (Th4+ concentration = 20 mg/L; reaction time = 15h; EPS dosage = 30mL).

Figure 6

Effect of different pH on Th4+ removal (Th4+ concentration = 20 mg/L; reaction time = 15h; EPS dosage = 30mL).

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Effect of initial concentration of Th4+

The removal efficiency and adsorption capacities for Th4+ adsorption onto EPS are given in Figure 7 as a function of the initial Th4+ concentrations. As seen in Figure 7, the adsorption capacities increased with increasing initial Th4+ concentrations as a result of the increase in the driving force. The removal efficiency of Th4+ adsorption by EPS decreased from 84.02 to 70.13% as the initial Th4+ concentration was increased from 10 to 50 mg/L. At lower Th4+ concentrations, all Th4+ present in the solution could interact with the binding sites and thus the removal efficiency was higher than those at higher initial Th4+ concentrations. At higher concentrations, lower removal efficiency is due to the saturation of adsorption sites. As an experiment result, the available sites on the surface of EPS are the limiting factor for Th4+ adsorption. Considering that the initial concentration of Th4+ is 20 mg/L, its removal effect is great, therefore this concentration is used for subsequent experiments.
Figure 7

Effect of Th4+ initial concentration on Th4+ removal (pH = 3.5; reaction time = 15h; EPS dosage = 30mL).

Figure 7

Effect of Th4+ initial concentration on Th4+ removal (pH = 3.5; reaction time = 15h; EPS dosage = 30mL).

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Effect of EPS dosage

The EPS dosage was investigated at 25 °C over the range (10 ∼ 60 mL). As shown in Figure 8, in terms of overall changes, with the increase in EPS dosage, the Th4+ removal efficiency increased, and the adsorption capacities of EPS decreased. The removal efficiency of Th4+ increases from 39.58 to 76.15% with raising the EPS dosage from 10 to 60 mL. It could be ascribed to the larger amount of adsorption sites provided by the increasing EPS dosage. By contrast, the adsorption capacities of the EPS decreased from 46.43 to 13.97 mg/g with the increasing EPS dosage. This is because with the increase in the amount of adsorbent, the polymer chain structure of the adsorption site was embedded and did not play the adsorption role (Zheng 2008). In addition, the strength of the binding site on the surface of the adsorbent is different, so the competitive adsorption of metal ions between the adsorbents will also lead to the reduction of the unit adsorption capacity.
Figure 8

Effect of EPS dosage on Th4+ removal (Th4+ concentration = 20 mg/L; reaction time = 15h; pH = 3.5).

Figure 8

Effect of EPS dosage on Th4+ removal (Th4+ concentration = 20 mg/L; reaction time = 15h; pH = 3.5).

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Notably, when the EPS is 30 mL, the Th4+ removal efficiency curve has an inflection point. Before this inflection point, the Th4+ removal efficiency increased with the increase in EPS dosage. After this inflection point, the increase in the EPS dosage did not obviously increase the Th4+ removal efficiency. Thus, 30 mL as best dosing quantity was applied in the subsequent experiments.

Effect of reaction time

The changes in removal efficiency of Th4+ with reaction time are shown in Figure 9. The process of Th4+ removal and Th4+ adsorption by EPS could be divided into three stages. In the first rapid adsorption stage (0 ∼ 2 h), the removal efficiency of EPS quickly increased to 36.3%. This phenomenon indicated that the utilization of the abundant binding sites on the surface of EPS to adsorb Th4+ was extremely rapid. In the second slow adsorption stage (2 ∼ 9 h), the Th4+ removal rate slowly increased to 75.46%. In the third stage of adsorption equilibrium (9 ∼ 13 h), the Th4+ removal efficiency of EPS basically no longer increased.
Figure 9

Effect of contact time on removal efficiency (Th4+ concentration = 20 mg/L; pH = 3.5; EPS dosage = 30mL).

Figure 9

Effect of contact time on removal efficiency (Th4+ concentration = 20 mg/L; pH = 3.5; EPS dosage = 30mL).

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Adsorption isotherms of EPS

Langmuir isotherm model is mainly used to study the maximum monolayer adsorption Freundlich isotherm model is usually better to describe the adsorption in aqueous solution (Xiong et al. 2009).

The Th4+ adsorption isotherms of EPS were described by classical Langmuir and Freundlich models.

The linear and nonlinear expressions of the Langmuir isotherm are as follows:
(3)
(4)
where Ce is the equilibrium concentration of Th4+ (mg/L) in solution, qe is the amount of Th4+ adsorbed at equilibrium, mg/g, qmax is the theoretical maximum adsorption capacity, mg/g, b is a constant related to the energy or net enthalpy of adsorption, L/mg.
The linear and nonlinear expressions of the Freundlich isotherm are as follows:
(5)
(6)
where k and n are Freundlich constants representing adsorption capacity (L/mg) and adsorption intensity, respectively. The values of between 0 and 1 suggest favorable adsorption (Hamane et al. 2015).
Experiments were performed at different temperatures (15, 25, and 30 °C) at a Th4+ concentration of 20 mg/L, EPS dosage of 30 mL at pH = 3.5, and a contact time of 15 h. The linearized and non-linearized Langmuir and Freundlich adsorption isotherms of Th4+ obtained are given in Figure 10. The evaluation of the isotherms at different temperatures with the correlation coefficients is also presented in Table 3. Comparing the correlation coefficients, it can be concluded that the Langmuir and Freundlich isotherms fit the experimental data better for the considered adsorption system. This indicates that in the adsorption process, there is a certain van der Waals force between EPS and Th4+ and the physical adsorption occurs in monolayer molecules on the surface of EPS. The calculated by the Freundlich equation were between 0 and 1, confirming the adsorption of Th4+ onto the EPS was favorable. The k value reflects the affinity of the adsorption system with metal ions. The k value of 8.55 ∼ 11.11 indicates EPS has a strong affinity for Th4+ in the aqueous environment (Wang et al. 2008).
Table 3

Linear and non-linear fitting parameters of Langmuir and Freundlich adsorption isotherm models

Typeθ/°CLangmuir
Freundlich
b/(L/mg)qmax/(mg/g)R2k/(L/g)R2
Linear 15 0.2700.0121 28.8110.00141 0.9676 8.5520.159 0.6510.0767 0.9632 
25 0.2560.0139 30.1290.0012 0.9364 9.08230.0088 0.6320.0432 0.9903 
30 0.6580.0118 31.2190.0014 0.9627 9.2730.0791 0.6610.0388 0.9873 
Non-linear 15 0.09370.0169 28.1470.0870 0.9875 11.1090.122 0.9520.0499 0.9883 
25 0.06980.117 30.9270.0134 0.9944 10.01610.177 0.03790.0685 0.9754 
30 0.07810.0187 30.2240.118 0.9887 10.4720.241 0.6070.0868 0.9524 
Typeθ/°CLangmuir
Freundlich
b/(L/mg)qmax/(mg/g)R2k/(L/g)R2
Linear 15 0.2700.0121 28.8110.00141 0.9676 8.5520.159 0.6510.0767 0.9632 
25 0.2560.0139 30.1290.0012 0.9364 9.08230.0088 0.6320.0432 0.9903 
30 0.6580.0118 31.2190.0014 0.9627 9.2730.0791 0.6610.0388 0.9873 
Non-linear 15 0.09370.0169 28.1470.0870 0.9875 11.1090.122 0.9520.0499 0.9883 
25 0.06980.117 30.9270.0134 0.9944 10.01610.177 0.03790.0685 0.9754 
30 0.07810.0187 30.2240.118 0.9887 10.4720.241 0.6070.0868 0.9524 
Figure 10

Linear (a) and non-linear (b) of Langmuir adsorption isotherm models, linear (c) and non-linear (d) of Freundlich adsorption isotherm models.

Figure 10

Linear (a) and non-linear (b) of Langmuir adsorption isotherm models, linear (c) and non-linear (d) of Freundlich adsorption isotherm models.

Close modal

The better adsorption capacity of Th4+ might be due to the presence of various functional groups at the surface of EPS which can attach to Th4+ via physicochemical interactions. This also confirms the conclusion obtained by FTIR spectral analysis in section 3.2.1.

In order to further explore the thermodynamic mechanism of EPS adsorption on Th4+, the adsorption process was analyzed. The thermodynamic parameters: free energy (ΔG), enthalpy (ΔH), and entropy (ΔS) change of Th4+ adsorption are evaluated from the following equations:
(7)
(8)
(9)
(10)
where K0 is the distribution coefficient for adsorption, L/g; R is the universal gas constant, 8.314 J/(mol·K); T is the absolute temperature, K. ΔS and ΔH are deduced from the intercept and slope of the linear plot of versus .

The parameters ΔG, ΔS and ΔH are listed in Table 4.

Table 4

Thermodynamics parameters for the adsorption of Th4+ by EPS

T/KΔG/(kJ/mol)ΔH/(kJ/mol)ΔS/[J/(mol·K)]
288 −4.914   
298 −5.065 39.381 152.669 
303 −7.613   
T/KΔG/(kJ/mol)ΔH/(kJ/mol)ΔS/[J/(mol·K)]
288 −4.914   
298 −5.065 39.381 152.669 
303 −7.613   

It can be seen from Table 3 that the Th4+ adsorption increases slightly from 28.81 to 31.22 mg/g with increasing temperature from 15 to 30 °C, indicating an endothermic process. Also, the positive value of ΔH confirms the heat-absorbing nature of EPS adsorption and the negative ΔG at different temperatures indicates spontaneous adsorption. Furthermore, the decrease of ΔG with an increasing temperature suggests that the adsorption is more favorable at higher temperatures. The positive value of ΔS indicates that the confusion degree of the system increases, reflecting the affinity of EPS for Th4+.

From the perspective of energy conservation, all experiments were carried out at 25 °C.

Adsorption kinetics of EPS

Pseudo-first-order, and pseudo-second-order kinetic equations were used to conduct the adsorption kinetics of EPS in the sorption process to analyze the adsorption mechanism.

The linear and nonlinear expressions of the pseudo-first-order dynamics model are as follows:
(11)
(12)
where qe and qt are the amounts of Th4+ adsorbed at equilibrium and at time t, respectively, mg/g. k1 is the pseudo-first-order rate constant, .
The linear and nonlinear expressions of the pseudo-second-order dynamics model are as follows:
(13)
(14)
where k2 is the pseudo-second order rate constant, mg/(g · h).
The fitting results are listed in Table 5 and illustrated in Figure 11. The correlation coefficients (R2) of the pseudo-second-order equation closed to 1, while that of the pseudo-first-order equation was low. The calculated qe (33.047 mg/g) values in the case of the pseudo-second-order equation also agreed with the experimental data. These results indicated that the EPS adsorption system is well described by the pseudo-second-order model, based on the assumption that the rate-limiting step may be chemisorption involving valency forces through sharing or exchange of electrons between adsorbent and adsorbate (Özer et al. 2004). This is similar to the results of the study by Xu et al. (2021). And the polysaccharides content in EPS is higher than proteins, which indicates that the adsorption rate of polysaccharides in EPS is faster than that of proteins.
Table 5

Parameters of linear and non-linear pseudo-first-order kinetics and pseudo-second-order kinetics

TypePseudo-first-order kinetics
Pseudo-second-order kinetics
qe/(mg/g)k1/hR12qe/(mg/g)k2/(g/mg·h)R22
Linear 28.4160.152 0.2300.0201 0.9425 33.0470.0097 0.00990.0013 0.9825 
Non-linear 27.5470.753 0.2770.0241 0.9895 33.7870.568 0.009180.0003 0.9837 
TypePseudo-first-order kinetics
Pseudo-second-order kinetics
qe/(mg/g)k1/hR12qe/(mg/g)k2/(g/mg·h)R22
Linear 28.4160.152 0.2300.0201 0.9425 33.0470.0097 0.00990.0013 0.9825 
Non-linear 27.5470.753 0.2770.0241 0.9895 33.7870.568 0.009180.0003 0.9837 
Figure 11

A Linear (a) and non-linear (b) of pseudo-first-order kinetic models, linear (c) and non-linear (d) of pseudo-second-order kinetic models.

Figure 11

A Linear (a) and non-linear (b) of pseudo-first-order kinetic models, linear (c) and non-linear (d) of pseudo-second-order kinetic models.

Close modal
The adsorbate species are most probably transported from the bulk of the solution into the solid phase through intra-particle diffusion/transport process, which is often the rate-limiting step in many adsorption processes (Özer et al. 2004). In order to further study the rate limiting steps of EPS adsorption behavior on Th4+, the intra-particle diffusion of Th4+ adsorption by EPS was explored by using the intra-particle diffusion model. The intra-particle diffusion equation is as follow:
(15)
where k3 is the diffusion rate constant in particles, g/(mg·); C is the diffusion constant within the particle, g/(mg·).
The intra-particle diffusion equation was used to fit the data of EPS adsorption of Th4+, the results are shown in Figure 12. It can be seen from Figure 12 that EPS adsorption process of Th4+ can be divided into three stages according to the intra-particle diffusion process, and the slope k3 of the three stages decreases with the increase of time, indicating that the adsorption amount gradually decreases and finally reaches equilibrium. The previous research has shown that if the intra-particle diffusion is the sole rate limiting step, it is essential for the plot qt versus to pass by the origin, which is not the case in this experiment (Özer et al. 2004). The plots present multi-linearity, this indicates the intra-particle diffusion involved in the Th4+ adsorption by EPS, but is not the sole rate-controlling-step.
Figure 12

Fitting curves for intra-particle diffusion of EPS adsorbed Th4+.

Figure 12

Fitting curves for intra-particle diffusion of EPS adsorbed Th4+.

Close modal
  • 1.

    The ultrasonic extraction method has the best effect on extracting EPS from indigenous bacteria of rare earth tailings, and the physical extraction method is generally more efficient than the chemical extraction method.

  • 2.

    The key factor of EPS adsorbed Th4+ was functional groups, including amide I and amide II of proteins, C–H from aliphatic, as well as O–H and C = O from carboxylic acid.

  • 3.

    The hydrophobic interaction of tryptophan and tyrosine in EPS plays an important role in the adsorption process.

  • 4.

    The pH, initial Th4+ concentration, and EPS dosage affected the equilibrium uptake of Th4+ to EPS, and the optimum pH, initial Th4+ concentration, and EPS dosage were determined as 3.5, 20 mg/L, and 30 mL, respectively.

  • 5.

    An increase in the adsorption of Th4+ deals with increasing temperature up and then followed by an exothermic uptake process at higher temperatures.

  • 6.

    The Langmuir and Freundlich adsorption models were applied to describe the experimental data. Equilibrium data fitted very well to both the Langmuir and Freundlich isotherm models.

  • 7.

    The kinetic data adsorption of EPS to Th4+ was found to follow the pseudo-second-order model. Chemical adsorption is the main adsorption mechanism.

The authors wish to thank the Natural Science Foundation of Inner Mongolia Autonomous Region of China (No. 2020MS02015, No. 2020MS0547), the National Natural Science Foundation of China (No. 42167029), the Open Program of Tianjin Key Laboratory of Green Chemical Engineering Proceed Engineering of Tianjin University (GCEPE20190108) for their support of this study.

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

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

The authors declare there is no conflict.

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