Shuli Liua,
Zhengyang Duana,
Changhua Hea,
Xiaojun Xu*a,
Tianguo Lib,
Yuhuan Lib,
Xuan Lia,
Yao Wanga and
Longqian Xua
aFaculty of Environmental Science and Engineering, Kunming University of Science and Technology, Kunming, Yunnan 650500, China. E-mail: xuxiaojun88@sina.com; Tel: +86-13577132038
bCollege of Resources and Environment, Yunnan Agricultural University, Kunming, Yunnan 650201, China
First published on 20th February 2018
Phosphate-modified baker's yeast (PMBY) was prepared, and used as a novel bio-sorbent for the adsorption of Pb2+ from aqueous solution. The influencing factors, absorption isotherms, kinetics, and mechanism were investigated. The scanning electron microscopy (SEM), Fourier-transform infrared spectroscopy (FTIR) characterization and elemental analysis of PMBY showed that phosphate groups were successfully grafted onto the surface of yeast. The kinetic studies suggested that the adsorption process followed a pseudo-second-order chemisorption. The adsorption process of Pb2+ using PMBY was spontaneous and endothermic. Furthermore, the adsorption of Pb2+ on PMBY can rapidly achieve adsorption equilibrium (in just 3 min), and the maximum adsorption capacity of Pb2+ on PMBY was found to be 92 mg g−1 at 30 °C, which was about 3 times that of the pristine baker's yeast. The suggested mechanism for Pb2+ adsorption on PMBY was based upon ion-exchange, electrostatic interaction and chelation between the phosphate groups and Pb2+. However, compared with the pristine baker's yeast, the higher capacity and rapid adsorption of PMBY for Pb2+ was mainly due to the chelation and electrostatic interactions between the phosphate groups and Pb2+. In addition, the regeneration experiments indicated that the PMBY was easily recovered through desorption in 0.01 M HCl, and that PMBY still exhibited 90.77% of the original adsorption capacity for Pb2+ after five regeneration cycles. These results showed the excellent regeneration capability of PMBY for Pb2+ adsorption. PMBY has shown significant potential for the removal of heavy metals from aqueous solution due to its rapid adsorption, high-capacity and facile preparation.
Considering the hazards associated with lead, a method involving highly efficient separation and recovery of lead from contaminated water is of great significance not only for the full utilization of lead resources, but also to protect the human health and ecological environment. Many methods have been used to treat wastewater containing lead, including chemical precipitation, electrochemical treatment, reduction, ion-exchange, solvent extraction, adsorption and flotation.8–10 There are some disadvantages associated with most of these methods, which restrict their application. These disadvantages include low efficiency, high energy consumption, large quantity of toxic and expensive materials used, and production of large amounts of sludge, which needs secondary treatment in some methods.8,11 Nevertheless, bio-adsorption has attracted considerable attention due to its environment-friendly nature and low cost. Additionally, bio-adsorption can effectively remove soluble and insoluble pollutants without generating hazardous by-products.12
Various microorganisms, such as bacteria, fungi and algae are a kind of bio-sorption materials, which can adsorb heavy metal ions.13–15 For bio-adsorption technology, the selection of appropriate biomaterial for the removal of hazardous heavy metals from aqueous solutions is a key process step.8 The source, safety, cost and adsorption capacity should be considered for the selection of any suitable biomaterial. Among the aforementioned biomaterials, yeast cells are frequently-used fungi, which often serve as suitable sources of bio-sorbent materials due to their easy cultivation, and have features such as inexpensive large-scale growth media, wide availability and safety.16,17 Previous researchers have demonstrated that the surface of yeast cells contains abundant amounts of functional groups, which can adsorb heavy metals, such as hydroxyl, carbonyl, and amide groups. However, the sorption capacities of yeast cells are still unsatisfactory due to limited surface functional groups.18 Therefore, it is necessary to improve the adsorption performance of yeast cells, especially with regards to the adsorption of lead. A number of modified strategies, such as the formation of nano-MnO2/nano-ZnO and hydroxyapatite on the yeast surface,19–21 modification of EDTAD/ethylenediamine/polymer,22–24 and pretreatment using ethanol/caustic have been proposed to improve the adsorption capacity of yeast.25 Surface modifications of yeast with organic and inorganic materials provide a hybrid material having higher efficiency and capacity for the removal of heavy metals by either introducing or exposing more surface functional groups on the surface of raw materials.26 Although, the aforementioned modifications of yeast improved the adsorption capacity for heavy metals, their relatively complicated synthesis and difficult procurement of preparation materials led to high costs. Therefore, synthesizing new bio-sorbents was more competitive and practical among various bio-sorbents, which have the capacity to sequester the heavy metal ions from aquatic environment. To achieve this, it is necessary to fabricate low-cost, reliable, rapid adsorption, durable and efficient materials. Among these properties, the rapid adsorption of bio-sorbents is one of the most serious problems hindering the commercial application of bio-sorbents. Many bio-sorbents need a long time to reach adsorption equilibrium, which would result in significant waste of energy and hence, reduce the treatment efficiency. Therefore, considering the adsorption rate while synthesizing a novel bio-sorbent is highly important for the overall efficiency of the adsorption process.
Phosphate is an inorganic material that is non-toxic and inexpensive. Phosphate groups are known to have excellent chelating properties for metal ions. Thus, many phosphorylated materials were applied to removal metal ions. For example, phosphorylated cellulose microspheres,27 phosphorylated chitosan,28 and phosphorylated starch have been used as adsorbents for metal ions removal.29 To the best of our knowledge, phosphate-modified baker's yeast has not been investigated in detail for the removal of lead from aqueous solutions. By forming hydroxyapatite on the surface of yeast, the functional groups of pristine yeast do not participate in the synthesis reaction. In other words, it is worth studying whether the phosphate-modified baker's yeast, which via the interaction between the phosphate and surface functional groups of baker's yeast, is a feasible and effective means to obtain an efficient and cheap bio-sorbent for Pb2+ or not.
Herein, a phosphate-modified baker's yeast (PMBY) was prepared using a simple pathway that involved phosphate treatment of baker's yeast and dry-heating. Then, the adsorption characteristics, kinetics, and isothermal behavior of PMBY for Pb2+ adsorption from aqueous solution were explored. Subsequently, a comparative analysis along with the scanning electron microscopy (SEM), Fourier-transform infrared spectroscopy (FTIR), and X-ray photoelectron spectroscopy (XPS) analyses were conducted to further explore the adsorption performance and mechanism of PMBY.
Various chemicals and reagents, including sodium dihydrogen phosphate (NaH2PO4·2H2O), sodium hydrogen phosphate (Na2HPO4·12H2O), sodium hydroxide (NaOH), nitric acid (HNO3), lead nitrate (Pb(NO3)2), and ammonium molybdate ((NH4)6Mo7O24·4H2O) were purchased from Aladdin-Biochemical Technology Co., Ltd., China. All these chemicals were of analytical reagent grade, and used without further purification. Lead nitrate was employed as the Pb2+ source. The stock standard solution of Pb(NO3)2 was obtained from the National Analysis Center for Iron and Steel (Beijing, China). The working solutions were obtained by diluting the stock solution. Furthermore, 1 M NaOH and 1 M HNO3 were used to adjust the pH values. All solutions were prepared using deionized water.
The morphology and the elemental composition of the samples were studied using tungsten filament scanning electron microscopy (SEM) and energy dispersive spectrometer (EDS) (JSM-7500F, Japan), operated at 20 kV acceleration voltage. Fourier-transform infrared spectra (FTIR) was observed using a PerkinElmer spectrometer (L1600400 spectrum Two DTGS, USA), which used potassium bromide (KBr) pellets. The mass ratio of potassium bromide to sample was 700:1, respectively. The FTIR analysis was obtained within the range of 400–4000 cm−1.30,31 The elemental analyses (C, H, O and N) were performed on an elemental analyzer (Elementar Vario Micro Cube, Germany). Moreover, the phosphorus content was assayed following the Chinese National Standard (GB 5009.268-2016), and was analyzed using a UV/Vis spectrophotometer (UV-VIS752, China) at 660 nm wavelength. X-ray photoelectron spectroscopy (XPS) was used to analyze the surface elemental composition of the samples. The measurements were carried out using Kratos Axis Ultra DLD (SHIMADZU, Japan) at room temperature. The ejected photoelectrons used a monochromatic beam of Al Kα X-rays (hν = 1486.6 eV) and the resulting binding energy peaks were referenced to C1s peak occurring at 284.8 eV. N2 adsorption–desorption isotherms were measured using a surface area analyzer (JW-BK132F, China). The specific surface area and pore size distribution of the samples were determined using Brunauer–Emmett–Teller (BET) method and Barrett–Joyner–Halenda (BJH) model.
The removal efficiency and the adsorption capacity of PMBY for Pb2+ were represented by R (%) and qe (mg g−1), respectively, and were calculated using eqn (1) and (2), respectively.
(1) |
(2) |
Fig. 2 SEM images and EDS spectra of pristine baker's yeast (a and b), PMBY (c and d) and PMBY-Pb (e and f). |
Fig. 3a shows the FTIR spectra of baker's yeast and PMBY. The FTIR spectra of pristine baker's yeast consisted of typical peaks of hydroxyl (3298.15 cm−1),20 carboxyl (1384.29 cm−1),24 amine-I (1654.54 cm−1), amide-II (1541.63 cm−1), amide-III (1239.31 cm−1), and phosphate groups (1048.02 cm−1).32–34 Compared with the pristine baker's yeast (shown in Fig. 3a), some changes were observed in the FTIR spectra of PMBY. The peaks at 828.09 and 615.76 cm−1 represented the P–O–C aliphatic bonds and symmetric stretching vibration of PO4, respectively.27,35 The new peaks at 828.09 and 615.76 cm−1 coincided with the phosphate group,36 and the two peaks at 1048.02 and 1076.32 cm−1 presented in the pristine baker's yeast merged into one peak at 1071.86 cm−1, which was assigned to P–O vibration, while its intensity increased remarkably.37 These changes indicated that the phosphate groups were successfully grafted on the surface of yeast. Besides, the peak height and peak band of hydroxyl, carboxyl and amine groups of pristine baker's yeast changed after the phosphate modification, which indicated that these groups had participated in the reaction.
Fig. 3 (a) FTIR spectra of pristine baker's yeast, PMBY and PMBY-Pb. (b) XRD patterns of pristine baker's yeast and PMBY. |
The phosphate groups, which were linked to the yeast, may have appeared due to either the substitution reaction or the ligand exchange process between the O–H group of hydroxyl groups and carboxylic acids, and phosphate. This can be represented using reaction eqn (3)–(6).
R–OH + HPO42− → R–O–PO32− + H2O | (3) |
R–OH + H2PO4− → R–O–HPO3− + H2O | (4) |
R–COOH + HPO42− → R–CO–O–PO32− + H2O | (5) |
R–COOH + H2PO4− → R–CO–O–HPO3− + H2O | (6) |
Additionally, the amine groups and phosphate groups could react through electrostatic attraction and hydrogen bonding.
The XRD patterns of pristine baker's yeast and PMBY composites are shown in Fig. 3b. Pristine baker's yeast presented a broad strong peak at about 2θ of 20°. In contrast to the pristine baker's yeast, the PMBY composites not only showed stronger diffraction pattern at about 2θ of 20°, but also exhibited few well-defined peaks involving crystal phosphate. These results suggested that the phosphate in PMBY composites may be in a non-stoichiometric and amorphous phase.20 The results were assigned to the content of phosphate in PMBY, which did not reach XRD's detection limit (5 wt%), whereas the crystallization of these was poor and not within the detectable range.38
The elemental analysis of the samples show that PMBY contains 45.02% C, 34.470% O, 8.160% H, 8.41% N and 0.53% P, respectively. The contents of C and H of PMBY decreases by comparing with pristine baker's yeast (C: 39.01%, O: 41.135%, H: 7.363%, N: 8.36%, P: 4.06%), while the contents of O and P increase significantly after reacting with phosphate. The results confirm that PMBY had been successfully synthesized.
qt = qe(1 − e−k1t) | (7) |
(8) |
C0 (mg L−1) | Experimental (mg g−1) | Pseudo-first-order | Pseudo-second-order | ||||
---|---|---|---|---|---|---|---|
K1 | qe | r2 | K2 | qe | r2 | ||
50 | 55.20 | 6.71 | 52.67 | 0.9724 | 0.27 | 54.31 | 0.9907 |
100 | 83.41 | 6.67 | 79.34 | 0.9713 | 0.18 | 81.84 | 0.9902 |
150 | 87.11 | 6.71 | 83.14 | 0.9725 | 0.17 | 85.72 | 0.9908 |
The calculated correlation coefficient values (r2) for pseudo-first-order and pseudo-second-order kinetics were found to be higher than 0.97, which show that both kinetic models can be used to predict the adsorption behavior of Pb2+ using PMBY for the entire contact time (Table 1). The predicted qe values at different Pb2+ concentrations using pseudo-second-order model were in a better agreement with the experimental values than the pseudo-first-order, which indicated that the adsorption process could be explained using pseudo-second-order model, while the adsorption rate was controlled by chemisorption.41–43 In addition, the pseudo-second-order rate constant (k2) decreased as the Pb2+ concentration increased from 50 to 150 mg L−1, suggesting that it took longer to achieve the adsorption equilibrium at higher Pb2+ concentrations, which may have been due to the limited number of available active sites on PMBY.
It is interesting to observe that, PMBY not only efficiently removed Pb2+ from the aqueous solution, but it also resulted in a better and faster removal rate than some other bio-sorbents. In order to display the advantage of PMBY, the maximum adsorption capacity of PMBY at 30 °C and the equilibrium time were compared with various yeast-based bio-sorbents used for Pb2+ adsorption (Table 2). The results indicated that the PMBY had relatively better adsorption capacity than the most of reported yeast-based bio-sorbents. Although the adsorption capacity of PMBY is lower than some bio-sorbents reported in literature (Table 2), the adsorption equilibrium time was very short compared with other reports. The rapid adsorption of PMBY makes it competitive to various other bio-sorbents.
Bio-sorbents | Biosorption capacity (mg g−1) | Equilibrium time (min) | Reference |
---|---|---|---|
Bakers' yeast | 28.45 | 30 | This work |
PMBY | 91.53 | 3 | This work |
Nano-ZnO/yeast composites | 31.72 | 30 | 19 |
HAP/yeast biomass composites | 48.93 | 60 | 21 |
EMB | 99.26 | 30 | 22 |
Ethanol treated baker's yeast | 17.49 | 120 | 44 |
Polymer modified baker's yeast | 203.06 | 20 | 45 |
Cystine-modified yeast | 45.87 | 20 | 46 |
EYMC | 127.37 | 60 | 23 |
Waste beer yeast | 5.72 | 60 | 47 |
To describe the sorption characteristics of PMBY more adequately, the equilibrium data from Fig. 5b was modeled using Langmuir and Freundlich isotherm models.48
The Langmuir isotherm model assumes homogeneous adsorption during the adsorption process. The Langmuir isotherm can be expressed using eqn (9).
(9) |
The Freundlich isotherm model assumes a heterogeneous adsorption, and infers that the heavy metal ions, which have been bided on the surface sites, may affect the adjacent sites. The Freundlich isotherm is represented by eqn (10).
qe = KFCe1/n | (10) |
Fig. 5b and Table 3 display the fitting results for Langmuir and Freundlich models, and show that the Langmuir isotherm could fit the equilibrium data better than the Freundlich isotherm. Firstly, the Langmuir isotherm resulted in a higher correlation coefficient (r2 > 0.98) than the Freundlich isotherm (r2 < 0.81). Secondly, the qm values (87.39, 91.53, 96.06 and 99.56 mg g−1 at 25, 30, 35 and 40 °C, respectively) obtained using the Langmuir isotherm coincided well with the experimental values. Therefore, it can be said that the sorption process was mainly monolayer sorption of Pb2+ onto the homogenous surface of PMBY.
T (°C) | qe (mg g−1) | Langmuir | Freundlich | ||||
---|---|---|---|---|---|---|---|
qm (mg g−1) | KL (L mg−1) | r2 | KF [(mg g−1) (L mg−1)1/n] | n | r2 | ||
25 | 84.26 | 87.39 | 0.2411 | 0.9857 | 38.6079 | 6.0295 | 0.7541 |
30 | 88.69 | 91.53 | 0.2834 | 0.9915 | 41.5128 | 6.1472 | 0.7627 |
35 | 93.85 | 96.06 | 0.3383 | 0.9959 | 44.5716 | 6.2263 | 0.7825 |
40 | 98.78 | 99.56 | 0.4922 | 0.9883 | 49.3750 | 6.6287 | 0.8004 |
Consequently, the Langmuir isotherm was further analyzed using the dimensionless constant, which was named as the equilibrium parameter or separation factor, and expressed as RL. RL can be calculate using eqn (11).6,8
(11) |
Various RL values represent four kinds of adsorption characteristics, which are as follows: unfavorable (RL > 1), linear (RL = 1), favorable (0 < RL < 1) and irreversible (RL = 0)
Based upon the temperature and initial lead ion concentrations used in this work, RL values were calculated, and it was found that, all of them ranged between 0–1 (Fig. 6), confirming that the sorption of Pb2+ by PMBY was favorable.
ΔG = −NTlnK | (12) |
(13) |
ΔG = ΔH − TΔS | (14) |
Fig. 7 Plot of ΔG and T for the adsorption of Pb2+ using PMBY (C0 = 100 mg L−1, pH = 5.0, PMBY dosage = 0.08 g, V = 100 mL, t = 15 min and T = 25, 30, 35 and 40 °C). |
T (°C) | ΔG (kJ mol−1) | ΔH (kJ mol−1) | ΔS (J (mol−1 K−1) |
---|---|---|---|
25 | −1.92 | 25.56 | 92.09 |
30 | −2.32 | ||
35 | −2.79 | ||
40 | −3.30 |
Under different temperature conditions, the negative values of ΔG demonstrate that the adsorption of Pb2+ using PMBY was spontaneous, while the decreasing values of ΔG with increasing temperature (from 25 to 40 °C) reveal that the elevated temperature can promote the binding of Pb2+ onto the surface of PMBY sorbent. The positive values of ΔH confirm that the adsorption process was endothermic, and the sorption involved chemisorption as higher temperatures can promote the dissolution of lead ions and reduce the protonation of surface functional groups of the adsorbent to facilitate the chelation between Pb2+ and PMBY.8 The positive value of ΔS show that the randomness increased during the reaction, which was due to the destruction of hydration shell formed by water molecules on the surface of PMBY as the Pb2+ was bound on PMBY to make a number of water molecules enter the solution. All the thermodynamic parameters reflect that the bio-sorbent PMBY has an excellent affinity for Pb2+.
Fig. 8 (a) N2 adsorption–desorption isotherms of PMBY and PMBY-Pb, (b) XPS analysis of pristine baker's yeast, PMBY and PMBY-Pb. |
After the adsorption of lead ions, there were large number of bright precipitates on the surface of PMBY, while the composites displayed a dense and compact structure (Fig. 2c and e). The EDS pattern (Fig. 2d and f) showed that a new peak of Pb appeared, while that of Na disappeared on PMBY-Pb compared to the PMBY. These changes illustrated that the lead ions were indeed adsorbed on the surface of PMBY through the mechanism of ion-exchange. Furthermore, comparing the FTIR spectra of PMBY and PMBY-Pb (shown in Fig. 3a), two new peaks at 1010.17 and 657.69 cm−1 were assigned to P–O–Pb and metal–oxygen (metal-hydroxide), respectively.27,50 The characteristic peaks of phosphate group obviously shifted or became weaker, which demonstrated that the removal of Pb2+ was mainly due to the phosphate groups. The adsorption mechanism was further investigated using XPS analysis.
The XPS spectra of pristine baker's yeast, PMBY and PMBY-Pb are displayed in Fig. 8b. Both the phosphorus and lead were observed obviously (Fig. 8b), indicating that the phosphorylation reaction had occurred, and that the lead ions were adsorbed to the surface of PMBY. The high-resolution spectra of O1s, P2p, N1s and Pb 4f are shown in Fig. 9, whereas the proposed components and their binding energies are presented in Table 5. Comparing the O1s, P2p and N1s spectra of pristine baker's yeast and PMBY (Fig. 9a, b and c), some novel peaks emerged beside the original peaks of O-, P- and N-containing functional groups in pristine baker's yeast. The new peaks confirmed that phosphate groups were introduced on the surface of pristine baker's yeast. The different binding energies of C–O, OC–O, –NH2 from PMBY and pristine baker's yeast illustrated that the hydroxyl, carboxyl and amino groups reacted with the phosphate. The results were found to be consistent with the FTIR characterization.
Fig. 9 High-resolution spectra of O1s (a), P2p (b) and N1s (c) for the pristine baker's yeast, PMBY and PMBY-Pb, and the Pb 4f XPS spectra of PMBY-Pb (d). |
Valence state | Pristine baker's yeast | PMYC | PMYC-Pb | |||
---|---|---|---|---|---|---|
Proposed component | Binding energy (eV) | Proposed component | Binding energy (eV) | Proposed component | Binding energy (eV) | |
O1s | C–O19,24 | 532.95 | C–O | 532.81 | C–O | 532.70 |
OC–O19,24 | 532.34 | OC–O | 532.19 | OC–O | 532.08 | |
PO27 | 531.88 | PO | 531.21 | PO | 530.80 | |
— | — | O–P28 | 533.45 | O–P | 533.28 | |
P2p | PO28 | 133.56 | PO | 133.50 | PO | 133.31 |
— | — | P–O27,28 | 133.11 | P–O | 132.3 | |
N1s | NH2 (ref. 34) | 399.86 | NH2 | 399.9 | NH2 | 399.82 |
— | — | NH3+ (ref. 51) | 401.4 | NH3+ | 400.42 | |
Pb 4f | — | — | — | — | Pb 4f 5/2 (ref. 27) | 143.19, 142.66 |
— | — | — | — | Pb 4f 7/2 (ref. 27) | 138.33, 137.8 |
After the adsorption, the peaks of O-, P- and N-containing functional groups in PMBY showed variations in terms of binding energy. However, the reduction binding energies of PO and P–O were the most obvious, revealing that the phosphate groups were mainly involved in the adsorption of lead.
The Pb 4f spectrum for PMBY-Pb is depicted in Fig. 9d. The peaks at around 140 eV were assigned to Pb 4f due to the adsorption of Pb2+. The peaks at 143.19 and 138.33 could be assigned to Pb2+, indicating that the lead was loaded on the surface of PMBY through chelation. Moreover, the Pb 4f peaks were centered at 142.66 eV and 137.8 eV, which suggested that Pb2+ may have been absorbed in PMBY in the form of Pb–O–P through ion-exchange process. According to the XPS spectra of PMBY and PMBY-Pb, the Na peak disappeared in the spectra of PMBY-Pb, indicating that the adsorption process of PMBY for Pb2+ followed ion-exchange. This result was also confirmed by the results of SEM-EDS. In addition, it is well-known that the metal cations are typical Lewis acids and that the phosphate groups with low acid–base ionization equilibrium constant (pKa = 1–2) show typical Lewis base properties in a wide range of pH values.27 Therefore, based upon the Lewis acid–base theory, lead ions can interact with the phosphate groups through chelation and electrostatic interaction. Due to the successful introduction of phosphate groups and the interaction (ion-exchange, chelation and electrostatic attraction) between the phosphate groups and Pb2+, the adsorption performance of PMBY for Pb2+ significantly improved.
Fig. 10 shows the reaction scheme and the proposed schematic of the adsorption mechanism of PMBY for Pb2+. Firstly, the surface functional groups of baker's yeast cell walls, such as hydroxyl, carboxyl and amine groups, reacted with NaH2PO4/Na2HPO4. The detailed synthesis is shown in Fig. 1. The phosphate groups were linked to the yeast through substitution reaction or the ligand exchange process between the O–H group of hydroxyl groups and carboxylic acids, and the phosphate. Additionally, the amine groups and phosphate groups could react through electrostatic attraction and hydrogen bonding. After this reaction, the novel PMBY bio-sorbent was obtained and used to remove Pb2+ from aqueous solution. The phosphate groups, which were grated into the surface of pristine baker's yeast played a significant role during the adsorption process. As shown in Fig. 10, the PMBY efficiently removed Pb2+ from aqueous solution. The process mainly depended upon these interactions (ion-exchange, chelation and electrostatic attraction) between the phosphate groups and Pb2+. The adsorption mechanism could be confirmed using SEM, FTIR and XPS analyses.
The order of desorption for Pb2+ was found to be: HCl (89.85%) > HNO3 (77.42%) > H2SO4 (69.06%) (Fig. 11a). The better recovery of Pb2+ in 0.01 M HCl was due to the smaller sized Cl− ions in comparison to the NO3− and SO42− ions.8 Hence, the recyclability of PMBY for the adsorption of Pb2+ was confirmed using 0.01 M HCl solution. As can be seen from Fig. 11b, after five regeneration cycles, PMBY still exhibited 90.77% of the original adsorption capacity. Therefore, it can safely be said that the adsorption efficiency of PMBY towards Pb2+ was still satisfactory after several regeneration cycles, whereas HCl was used as the eluent during these regeneration experiments. All these results suggested that PMBY could act as a renewable and efficient adsorbent for the remediation of wastewater containing Pb2+.
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