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Article

Spirulina platensis Immobilized Alginate Beads for Removal of Pb(II) from Aqueous Solutions

by
Oyunbileg Purev
1,
Chulhyun Park
1,
Hyunsoo Kim
1,
Eunji Myung
2,
Nagchoul Choi
3 and
Kanghee Cho
3,*
1
Department of Energy and Resource Engineering, Chosun University, Gwangju 61452, Republic of Korea
2
Green-Bio Research Facility Center, Seoul National University, Seoul 25354, Republic of Korea
3
Research Institute of Agriculture and Life Sciences, Seoul National University, Seoul 08826, Republic of Korea
*
Author to whom correspondence should be addressed.
Int. J. Environ. Res. Public Health 2023, 20(2), 1106; https://doi.org/10.3390/ijerph20021106
Submission received: 24 December 2022 / Revised: 2 January 2023 / Accepted: 6 January 2023 / Published: 8 January 2023
(This article belongs to the Special Issue Organic Solid Waste Valorisation and Environmental Health)
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Versions Notes

Abstract

:
Microalgae contain a diversity of functional groups that can be used as environmental adsorbents. Spirulina platensis is a blue-green microalga that comprises protein-N, which is advantageous for use in nitrogen-containing biomass as adsorbents. This study aimed to enhance the adsorption properties of alginate hydrogels by employing Spirulina platensis. Spirulina platensis was immobilized on sodium alginate (S.P@Ca-SA) via crosslinking. The results of field-emission scanning electron microscopy, Fourier-transform infrared, and X-ray photoelectron spectroscopy analyses of the N-containing functional groups indicated that Spirulina platensis was successfully immobilized on the alginate matrix. We evaluated the effects of pH, concentration, and contact time on Pb(II) adsorption by S.P@Ca-SA. The results demonstrated that S.P@Ca-SA could effectively eliminate Pb(II) at pH 5, reaching equilibrium within 6 h, and the maximum Pb(II) sorption capacity of S.P@Ca-SA was 87.9 mg/g. Our results indicated that S.P@Ca-SA fits well with the pseudo-second-order and Freundlich models. Compared with Spirulina platensis and blank alginate beads, S.P@Ca-SA exhibited an enhanced Pb(II) adsorption efficiency. The correlation implies that the amino groups act as adsorption sites facilitating the elimination of Pb(II).

1. Introduction

In the last few decades, industrialization and urbanization have triggered serious environmental issues, with irreparable damage to the ecological environment and human health. Wastewater contaminated with heavy metals is generated in large quantities from natural resources, such as tailings, and diverse industries, including electroplating, smelting, battery and paint manufacture, coating, and mining [1,2,3]. For instance, in mining industries, mineral processing discharges a huge amount of wastewater comprising hazardous metal ions annually. Of the numerous heavy metals employed industrially, Pb(II) is highly toxic and has adverse effects that are injurious to human and animal health because it is bio-accumulative and non-biodegradable. It enters the body predominantly through the skin and food, leading to brain disorders, anemia, kidney disease, and other diseases [4]. Owing to its high toxicity and irreversible damage, South Korea recommends that the concentration of Pb(II) in industrial wastewater should not exceed 0.5 mg/L.
To date, many technologies involving physicochemical and biological approaches, including adsorption, chemical precipitation, and ion exchange, have been adopted to remove heavy metal ions from wastewater [5,6,7,8,9,10,11]. Among these, adsorption has been established as effective in eliminating heavy metal ions, and studies on diverse adsorbents are gaining attention [12,13]. Cost-effective adsorbent-based adsorption techniques have become promising treatment approaches in recent years because of their economic viability and environmental friendliness [14,15]. Currently, activated carbons are the most commonly available adsorbents for heavy metal elimination in wastewater treatment due to their highly porous structure, high specific surface area, and flexibility for surface modification [16]. However, coal-based activated carbons are expensive, and the subsequent pore blockage after heavy metal adsorption degrades their porous structure. Hence, the development of a cost-effective adsorbent that is not only renewable but also has high adsorption capability is the need of the hour.
A variety of agricultural and industrial wastes have been employed for the preparation of low-cost adsorbents. Adsorbents based on agricultural waste are considered cost-effective because of their diverse functional groups, including carboxyl, phenolic, and hydroxyl groups, and easy accessibility. However, the drawback of most waste-based adsorbents lies in the complexity of the adsorbent preparation process [17,18]. Additionally, these adsorbents are synthesized through thermal activation and chemical modifications [19,20].
In recent years, microalgae have captivated increasing attention owing to their simple cultivation and high biomass productivity [21,22]. Microalgae are photosynthetic organisms that are naturally abundant in many regions of the world [23]. Given the significance and rich sources of bioactive compounds with physiological effects, microalgae have drawn interest from researchers and food manufacturers because of their high protein and nutritional content. Moreover, they can be adopted as an adsorbent owing to their high biomass productivity [24]. Among the numerous microalgae species, Spirulina platensis is a blue-green microalga that comprises predominantly protein (55–70% of the total dry weight) and has a high nutritional value, including provitamin A, vitamins C and E, essential amino acids, and unsaturated fatty acids [25,26]. The key photosynthetic pigment of Spirulina platensis is the dense blue phycocyanin [17]. The surface layers of Spirulina platensis have multiple functional groups, including –COOH, –PO4, –OH, –SO4 –NH2, and –SH [27,28]. Therefore, the functional groups of Spirulina platensis can be employed for the sorption of heavy metals and dyes from aqueous solutions [21,22,23,24].
Considering this, microalgae-derived biochar with a high adsorption capacity is extensively exploited for adsorption studies, but its carbon content is lower than that of coal-based carbons [29,30,31,32]. Additionally, microalgae with low density or biochars are relatively limited, which is a challenge during separation after wastewater treatment [33,34]. This study aimed to enhance the properties of alginate hydrogels using microalgae. We selected Spirulina platensis as a low-cost adsorbent due to its enriched N-containing functional groups. More adsorption sites can be exposed, and stability can also be enhanced when sodium alginate composites with Spirulina platensis are utilized. Sodium alginate was synthesized using an in situ crosslinking process and adopted for Spirulina platensis immobilization. Sodium alginate–Spirulina platensis can create hydrogels via Ca2+ crosslinking, comprising more controllable particle size and plentiful functional groups, including amino, hydroxyl, and carboxyl groups. We evaluated the adsorption of lead from aqueous solutions of sodium alginate–Spirulina platensis.

2. Materials and Methods

2.1. Materials

Spirulina platensis powder was purchased from Qingdao Haixingyuan Biotechnology Co. Ltd. (Qingdao, China) The powder was washed thrice with distilled water to eliminate impurities and collected by centrifugation at 5000 rpm for 10 min. The washed powder was then dried overnight at 60 °C. The dried powder was pulverized and sieved using a standard sieve with a 200 mesh size. Sodium alginate (90%, SA) and calcium chloride (99%, CaCl2·2H2O) were obtained from Duksan Pure Chemicals (Ansan, Republic of Korea) and used to prepare alginate beads via Ca2+ crosslinking. Lead nitrate (99%, Pb(NO3)2), copper nitrate trihydrate (99%, Cu(NO3)2·3H2O), zinc nitrate hexahydrate (98%, Zn(NO3)2·6H2O), and cadmium nitrate tetrahydrate (98%, Cd(NO3)2·4H2O) were obtained from Daejung Chemical (Busan, Republic of Korea).

2.2. Immobilization of Spirulina platensis in Sodium Alginate

Spirulina platensis immobilized in sodium alginate was synthesized employing the following procedure. To minimize the salt content, Spirulina platensis powder was washed five times with distilled water and later dried for a period of 24 h at 100 °C in an oven. Spirulina platensis (2%, w/v) and SA (2%, w/v) were separately dissolved in deionized water and stirred to achieve uniform viscosity. After homogenization, the two solutions were mixed at a ratio of 1:1 and stirred overnight. Once homogeneous, the mixed slurries were incorporated into a solution containing 4% (w/v) CaCl2 using a peristaltic pump at a speed of 5 mL/min to form a spherical hydrogel based the bonding of the alginate group with Ca ions. The immobilized Spirulina platensis in sodium alginate (S.P@Ca-SA) remained in the aqueous solution for 1 h and was then washed with distilled water. Blank alginate beads were prepared using the same procedure as the S.P@Ca-SA beads, except for the inclusion of Spirulina platensis solution.

2.3. Characterization of Spirulina platensis and S.P@Ca-SA

The thermogravimetric behavior of Spirulina platensis was evaluated using TGA (SDT Q600, TA Instruments, New Castle, DE, USA). The analysis was conducted at a heating rate of 10 °C/min under N2 and a temperature range of 30–1000 °C. The surface functional groups of Spirulina platensis and S.P@Ca-SA were verified using a Fourier-transform infrared (FTIR) spectrometer (Nicolet 6700, Thermo Scientific, Waltham, MA, USA). The morphology and elements of the samples were detected using field-emission scanning electron microscopy (FE-SEM, S4800, Hitachi, Hitachi, Japan) with EDS (ISIS310, Jeol, Japan). The chemical bonding and elements were evaluated using X-ray photoelectron spectroscopy (XPS, Thermo Scientific K-Alpha spectrometer) with an X-ray source of Al Kα radiation. N2 adsorption-desorption isotherm evaluation was conducted using a surface area analyzer (BELSORP-max, BEL Japan Inc., Osaka, Japan). The zeta potentials under diverse pH conditions were characterized by zeta potential measurements using a Zetasizer Nano Analyzer (ZS 90, Malvern, UK).

2.4. Batch Experiments

To investigate the initial adsorption of Spirulina platensis, divalent metal solutions of Pb(II), Cu(II), Zn(II), and Cd(II) at a concentration of 100 mg/L were prepared, and adsorption experiments were conducted (adsorbent dose = 1 g/L, 24 h). The effects of S.P@Ca-SA dosage, kinetics, equilibrium isotherm, initial solution pH, and recyclability were examined. Duplicate tests were executed to ensure data quality, and the mean values were calculated with standard deviations less than 5%. The effluent concentration in the filtrate was estimated using ICP-OES (Perkin Elmer Optima Model 5300DV, USA).
The effects of initial solution pH on Pb(II) removal were assessed at pH levels ranging from 1 to 7. The solution pH was adjusted using 0.1 M NaOH and 0.1 M HCl solutions and was measured using a pH probe (9107BN, Thermo Scientific, Waltham, MA, USA). Kinetic experiments (adsorbent dose = 1, 5, and 10 g/L; initial Pb(II) concentration = 100 mg/L, pH 5.1) were conducted at reaction times ranging from 10 min to 24 h. Equilibrium isotherm experiments (adsorbent dose = 1, 5, and 10 g/L; reaction time = 3 h) were conducted at initial Pb(II) concentrations ranging from 10 to 100 mg/L. The regeneration of S.P@Ca-SA is imperative for augmenting the cost-effectiveness of the adsorption process. Recyclability experiments were performed for five cycles of adsorption–desorption. The adsorption experiment was performed using S.P@Ca-SA (adsorbent dose = 1 g/L) and Pb(II) (100 mg/L) for 6 h. For each cycle, the Pb(II)-adsorbed S.P@Ca-SA was reacted for 1 h with 0.1M NaOH solution.
Pb(II) removal capacity (qe, mg/g) was calculated with the following equation:
q e = C i − C f C a
where Ci is the Pb(II) concentration in the aqueous phase before the reaction (mg/L), Cf is the Pb(II) concentration in the aqueous phase post-reaction (mg/L), and Ca is the S.P@Ca-SA dose (g/L).
Kinetic adsorption data were analyzed using the following nonlinear forms of the pseudo-first-order (Equation (2)) and pseudo-second order (Equation (3)) models:
q t = q e [ 1 − exp ( − k 1 t ) ]
q t = k 2 q e 2 t 1 + k 2 q e t
where qt is the amount of adsorbed Pb(II) per unit mass of S.P@Ca-SA (g/L) at time t (mg/g), and qe is the amount of adsorbed Pb(II) per unit mass of S.P@Ca-SA (g/L) at equilibrium (mg/g). k1 is the pseudo-first-order rate constant (1/h), and k2 is the pseudo-second-order rate constant (g/mg/h).
The equilibrium sorption data were analyzed using the following nonlinear forms of Langmuir (Equation (4)) and Freundlich (Equation (5)) isotherm models:
q e = Q m K L C e 1 + K L C e
q e = K F C e n
where Qm is the maximum mass of adsorbed Pb(II) per unit mass of adsorbent (adsorption capacity, mg/g), and Ce is the concentration of Pb(II) in the aqueous solution at equilibrium (mg/L). KL is the Langmuir constant connected to the binding energy (L/mg), KF is the Freundlich distribution coefficient (L/g), and 1/n is the Freundlich constant.
The following equations for the determination of coefficient (R2), chi-square coefficient (χ2), and sum of the squared error (SSE) were used to analyze the adsorption data and confirm their fit to the model:
R 2 = ∑ i = 1 m ( y c − y e ¯ ) i 2 ∑ i = 1 m ( y c − y e ¯ ) i 2 + ∑ i = 1 m ( y c − y e ) i 2
χ 2 = ∑ i = 1 m [ ( y e − y c ) 2 y c ] i
SSE = ∑ i = 1 n ( y e − y c ) 2
where y c is the removal capacity calculated from the model, y e is the removal capacity measured in the experiment, and y e ¯ is the average measured removal capacity.

3. Results and Discussion

3.1. Characterization of Spirulina platensis

An EDS investigation was performed to identify the elemental characteristics of Spirulina platensis. Accordingly, Spirulina platensis was primarily composed of C (74.5 wt%), O (23.7 wt%), S (0.85 wt%), and K (0.82 wt%) (Figure 1a). Carbon was the key element, and some trace chemical elements were adsorbed on the surface, indicating that they were derived from the growing media. The TG and DSC curves of Spirulina platensis at a heating rate of 10 °C/min under an inert N2 atmosphere are represented in Figure 1b. Spirulina platensis had a total mass loss of 78.3%, and the highest mass loss (68.7%) occurred at 500 °C, which corresponds to the loss of moisture, and cellulose, lipid, and protein decomposition [35,36].
FTIR and XPS analyses were performed to verify the functional groups in Spirulina platensis. The FTIR spectrum of Spirulina platensis is presented in Figure 1c, demonstrating the presence of abundant functional groups on its surface. The FTIR spectrum indicated the presence of N-H and O-H (3400 cm−1), aliphatic C-H (3000–2900 cm−1), C=O (amide I, 1655 cm−1), and C-H stretching (1450 cm−1) accompanied by N-H binding (amide II, 1541 cm−1). A characteristic band was observed at approximately 1400–1000 cm−1 which was associated with S=O, C=C, C-O, and C-OH vibrations [37,38]. An evaluation of the XPS spectra was also performed to investigate the chemical composition of the surface of Spirulina platensis. The peaks at 284.4, 399.2, and 531.2 eV were assigned to C1s (73.6%), O1s (8.2%), and N1s (17.9%), respectively. In a high-resolution scan of N1s, the peak at 399.9 eV was attributed to protein-N (Figure 2) [39].
A preliminary adsorption study was conducted to explore the performance of Spirulina platensis dry biomass in heavy metal adsorption. The sorption properties of Spirulina platensis were assessed for Pb(II), Cu(II), Zn(II), and Cd(II) elimination with a 1.0 g/L adsorbent dose and an initial metal concentration of 100 mg/L. This was done to evaluate the heavy metal removal capacity. The capacity of Spirulina platensis for removal of metal cations was ranked as follows: Pb (68.0 mg/g) > Cd (34.8 mg/g) > Cu (30.0 mg/g) > Zn (26.1 mg/g) (as indicated in Figure 3a). The Pb removal capacities of various species of microalgae biomass reported in the literature are presented in Table 1. The adsorption capacity of heavy metals can be attributed to the plentiful functional groups, including amine, carboxyl, and hydroxyl groups, on the surface (Figure 3b). After Spirulina platensis adsorbed heavy metals, a decline in the OH stretching band intensity was confirmed. However, the metal cation removal by FTIR analysis indicated that there was no significant difference in the functional groups involved in the sorption process. Our results were similar to those of Ferreira et al. [40], who observed metal cation removal in Spirulina platensis using FTIR analysis. These studies have demonstrated that the functional groups involved in Pb(II) adsorption are the hydroxyl groups. Moreover, Spirulina platensis had an isoelectric point at pH 2.85 (Figure 3c). Thus, cationic metals can adsorb onto the negatively charged surface of Spirulina platensis through electrostatic interactions.

3.2. Characterization of SP@Ca-SA

Digital imaging established that calcium alginate was colorless, whereas S.P@Ca-SA was green. The morphology of S.P@Ca-SA was revealed using SEM, as depicted in Figure 4. Calcium alginate is spherically shaped and has a denser surface structure, whereas S.P@Ca-SA has an irregular surface and a more porous structure. The EDS of S.P@Ca-SA divulged the presence of C (59.5 wt%), O (36.9 wt%), Ca (2.12 wt%), and Cl (1.34 wt%). Post crosslinking of sodium alginate with calcium chloride, Ca and Cl were observed, indicating that alginate exists as a residue after crosslinking. The BET surface area of S.P@Ca-SA was determined to be 159.5 m2/g, which was higher than that of calcium alginate. Fila et al. (2022) reported that calcium alginate had a specific surface area of <5 m2/g [41]. It could be seen that S.P@Ca-SA had a more porous structure, implying the alterations in a greater number of sorption sites.
The spectra of calcium alginate (Ca-SA) and S.P@Ca-SA were compared to identify the functional groups. The FTIR spectrum of S.P@Ca-SA is presented in Figure 5a, indicating that Spirulina platensis was successfully immobilized on the alginate matrix. The functional groups characterized by calcium-crosslinked alginate hydrogels indicated the presence of stretching vibrations of the O-H groups (about 3320 cm−1) and the C-O asymmetric (1598 cm−1) and C-O symmetric (1427 cm−1) vibrations in the COO groups [42,43]. This result indicates that Ca in the CaCl2 solution intercalates through an ion-exchange reaction with Na in the sodium alginate. S.P@Ca-SA depicted a similar formation of functional groups, and novel characteristic peaks appearing for S.P@Ca-SA compared with calcium alginate. Among these peaks, those at 2854 and 2926 cm−1 were assigned to CH2 symmetric and CH2 asymmetric stretching, respectively, and those at 1541 and 1412 cm−1 were assigned to the N-H bending vibration. Furthermore, peaks at 1084 and 1027 cm−1 were identified as C-N and C-O stretching vibrations, respectively.
XPS spectra were evaluated to detect the functional groups present before and after the adsorption of Pb(II) ions onto S.P@Ca-SA. The wide scans of S.P@Ca-SA are depicted in Figure 5b; the characteristic peaks pre-adsorption at binding energies of 284.8, 399.1, and 531.4 eV are attributed to C1s, N1s, and O1s, respectively. Post adsorption of Pb(II), a new characteristic peak appeared at a binding energy of 138.3 eV, which was attributed to Pb 4f [44,45,46]. Compared with Pb(NO3)2, a lower binding energy of 139.6 eV for Pb 4f was observed, which was associated with the affinity of Pb(II) and S.P@Ca-SA [47]. The high-resolution spectra of N1s of S.P@Ca-SA are shown in Figure 6. The peaks at 399 and 400 eV were attributed to NH2 and NH3, implicating that Spirulina platensis successfully immobilized into alginate. After Pb(II) adsorption, the NH2 peak shifted to lower binding energies, indicating complexation between the NH2 groups and Pb(II). The peaks at 284.8, 286.4, and 288.0 eV in the C1s spectrum of S.P@Ca-SA were assigned to C-C, C-N, and O-C=O, respectively. The O1s spectrum exhibited peaks at 531.8, 532.5, and 533.4 eV, which were ascribed to C=O, C-O, and O-C=O, respectively. Compared with the XPS spectrum before Pb(II) adsorption, the spectra of both C1s and O1s demonstrated obvious changes after adsorption.

3.3. Adsorption Experiments

3.3.1. Effect of Initial pH on the Adsorption

The initial pH of Pb(II) plays a critical role in adsorption due to Pb speciation in the solution, surface charge, and competition for available sorption sites. To investigate the effect of pH, pH levels varying from 1 to 7 were established by adjusting the initial solution pH using 0.1 M NaOH or HCl. The major forms of Pb(II) present in aqueous solutions are dependent on pH [48,49]. Therefore, this initial pH range was selected to avoid precipitation of Pb(OH)2. The effects of initial pH on Pb(II) removal by S.P@Ca-SA are shown in Figure 7. As expected, Pb(II) adsorption onto S.P@Ca-SA depended on the pH value, and the removal capacity was augmented with increasing pH. Increasing doses of S.P@Ca-SA at pH 5 reduced the removal capacity from 87.9 to 9.98 mg/g. Under highly acidic conditions at pH 1, Pb(II) sorption declined sharply, which could be ascribed to the competition between Pb(II) and H+ ions for sorption sites [50]. This suggests the contribution of the effects of protonation or deprotonation of functional groups on the S.P@Ca-SA surface. Moreover, the zeta potential charge (pHZPC) of S.P@Ca-SA was found to be 1.17, which was related to the surface state of S.P@Ca-SA. When the solution pH was above pHZPC, the adsorption capacity of S.P@Ca-SA indicated that the influence of ionic groups, such as carboxylate, was more conducive to the adsorption efficiency of Pb(II).

3.3.2. Equilibrium Isotherms and Kinetic Model Analyses

The effect of the dose of S.P@Ca-SA on Pb(II) removal capacity was studied using an initial concentration ranging from 10 to 100 mg/L, with shaking for 180 min, and the results are represented in Figure 8a. With increasing doses of S.P@Ca-SA, the removal capacity of S.P@Ca-SA diminished (amount of Pb(II) adsorbed per unit mass), whereas the removal efficiency of Pb(II) was augmented. When the initial concentration was 100 mg/L, as the adsorbent dose increased from 1 to 10 g/L, the maximum removal capacity reduced from 30.5 to 9.60 mg/g. Additionally, the removal capacity of S.P@Ca-SA at 1 g/L dosage increased from 7.68 to 30.5 mg/g for Pb(II) as the initial concentration escalated. Our results demonstrate that the number of sorption sites available for Pb(II) was augmented, resulting in an enhanced removal capacity and availability for adsorption at higher concentrations. To analyze the type of Pb(II) adsorption, equilibrium isotherm models, including the Langmuir and Freundlich models, were adopted for data fitting. The equilibrium model parameters are listed in Table 2. The fitting results, as compared using the two equilibrium isotherm models, revealed that the Freundlich model is most suitable for describing the equilibrium data with parameter values of KF = 9.48–2.99 L/g and 1/n = 0.27–0.40.
The adsorption kinetics were examined with diverse doses of S.P@Ca-SA for Pb(II) removal at the initial concentration (C0 = 100 mg/L), and the results are depicted in Figure 8b. S.P@Ca-SA attained equilibrium after 6 h of contact with the Pb(II) solution. To evaluate the kinetic data in the study, kinetic sorption models, including pseudo-first-order and -second-order models, were fitted, and the error functions for R2, χ2, and SAE were employed to evaluate the experimental data. The calculated kinetic parameters and correlation coefficients are enlisted in Table 3. R2, χ2, and SSE values of the pseudo-second-order model were higher than those of the first-order model. Therefore, it is concluded that the pseudo-second-order model is more suitable for describing the kinetic data with parameter values of qe = 89.6–11.6 mg/g and k2 = 0.02–0.39 g/mg/h. The Pb removal capacities of various biomass-based adsorbents reported in the literature are presented in Table 4.

3.3.3. Recyclability of SP@Ca-SA

The regeneration ability of S.P@Ca-SA was studied using Pb(II) adsorption–desorption experiments. Herein, 0.1 NaOH was selected to regenerate the adsorbent. Post adsorption, equilibrium was attained (77.7 mg/g), and the adsorbed Pb(II) was desorbed at 87% within 60 min. A regeneration experiment with S.P@Ca-SA was conducted, as depicted in Figure 9. The Pb(II) adsorption capacity of S.P@Ca-SA was maintained at the same level even after five regeneration cycles, which indicates that S.P@Ca-SA can be reused with good durability.

3.4. Adsorption Mechanisms

Ca-SA and S.P@Ca-SA were compared to evaluate the effects of Spirulina platensis immobilization. Batch experiments were performed for divalent metal ion solutions, Pb, Cu, Zn, and Cd, at 100 mg/L concentration (Figure 10). Ca-SA had a relatively lower affinity for Pb(II) than S.P@Ca-SA. This implies that the enhanced adsorption capacity and selectivity were due to the introduction of alginate into the N-containing functional groups. Under the given experimental conditions, the Pb(II) removal capacity was the highest, while the relative removal efficiencies of several divalent metal ions tended to be low. A similar observation was reported by Zhang et al. (2020), who established that this tendency could be attributed to the stability constant of the associated metal acetate and hydroxide [57]. Other researchers have also reported that the contribution of competitive adsorption is influenced by electronegativity and ionic radius [58,59].
From the above FTIR and XPS results, Ca-SA had typical O-containing functional groups, including -OH and -COOH on the surface, indicating that Pb(II) adsorption was primarily electrostatic. Meanwhile, S.P@Ca-SA had N-containing functional groups, suggesting that the amino groups had an impact on Pb(II) removal. The Pb(II) adsorption capacity of S.P@Ca-SA was ascribed to complexation between the amino groups and Pb(II). This signifies that a stable coordination complex was formed by chelation between the amino groups and Pb(II). Compared with the XPS spectrum before Pb(II) adsorption, the change in the binding energies indicated that the N-containing functional groups (N1s) may participate in the removal process. Moreover, positively charged Pb(II) can adsorb onto the negatively charged carboxyl and hydroxyl functional groups present in S.P@Ca-SA through electrostatic interactions.

4. Conclusions

Spirulina platensis was incorporated using an in situ crosslinking process to the alginate matrix, which resulted in an increased Pb(II) adsorption capacity. The FTIR and XPS spectral patterns of S.P@Ca-SA verified that functional groups, including amine, carboxyl, and hydroxyl groups, were associated with the alginate matrix. For Spirulina platensis, Ca-SA, and S.P@Ca-SA, the maximum adsorbed amount of Pb(II) reached 68.0 mg/g, 80.5 mg/g, and 89.4 mg/g, respectively. Compared with Spirulina platensis and blank alginate beads, S.P@Ca-SA exhibited an enhanced Pb(II) adsorption efficiency. The improvement in Pb(II) adsorption with the immobilization of Spirulina platensis may be associated with functional groups and the availability of more adsorption sites. Batch experiments demonstrated that S.P@Ca-SA could effectively remove Pb(II) at pH 5, reaching equilibrium within 6 h, and the maximum Pb(II) sorption capacity of S.P@Ca-SA was 87.9 mg/g. Our results indicated that S.P@Ca-SA fits well with the pseudo-second-order and Freundlich models. The adsorption results demonstrated that complexation and electrostatic attraction could be the mechanism underlying Pb(II) adsorption. Overall, the regeneration efficiency of S.P@Ca-SA was excellent for up to five regeneration cycles. S.P@Ca-SA could be a promising adsorbent for the removal of Pb(II) from aqueous solutions.

Author Contributions

O.P.: Methodology and writing—original draft; C.P.: Funding acquisition; H.K.: Investigation; E.M.: Methodology; N.C.: Project administration; K.C.: Conceptualization, Writing—original draft and Writing-Reviewing and Editing. All authors have read and agreed to the published version of the manuscript.

Funding

This work was supported by the Korea Environment Industry & Technology Institute through “Project to develop eco-friendly new materials and processing technology derived from wildlife” funded by the Korean Ministry of the Environment (Grant number 2021003240001).

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

All data generated or analyzed during this study are included in this published article.

Conflicts of Interest

There is no conflict of interest to declare.

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Ijerph 20 01106 g001 550
Figure 1. Characteristics of Spirulina platensis: (a) EDS pattern (inset = chemical composition), (b) TGA, (c) FTIR spectrum, and (d) XPS survey spectra.
Figure 1. Characteristics of Spirulina platensis: (a) EDS pattern (inset = chemical composition), (b) TGA, (c) FTIR spectrum, and (d) XPS survey spectra.
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Figure 2. High resolution X-ray photoelectron spectroscopy (XPS) spectra for the surface of Spirulina platensis: (a) C 1 s (b) N 1 s and (c) O 1 s.
Figure 2. High resolution X-ray photoelectron spectroscopy (XPS) spectra for the surface of Spirulina platensis: (a) C 1 s (b) N 1 s and (c) O 1 s.
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Figure 3. (a) Effect of contact time on adsorption capacity of Pb(Ⅱ), Cu(Ⅱ), Zn(Ⅱ), and Cd(Ⅱ) ions. (b) Fourier-transform infrared spectroscopy of Spirulina platensis before (a) and after adsorption (b–e) (Note: Spirulina platensis after adsorption using Pb(b), Cd(c), Cu(d), and Zn(e), initial concentration of 100 mg/L, respectively). (c) Zeta potential as a function of pH for Spirulina platensis and S.P@Ca-SA.
Figure 3. (a) Effect of contact time on adsorption capacity of Pb(Ⅱ), Cu(Ⅱ), Zn(Ⅱ), and Cd(Ⅱ) ions. (b) Fourier-transform infrared spectroscopy of Spirulina platensis before (a) and after adsorption (b–e) (Note: Spirulina platensis after adsorption using Pb(b), Cd(c), Cu(d), and Zn(e), initial concentration of 100 mg/L, respectively). (c) Zeta potential as a function of pH for Spirulina platensis and S.P@Ca-SA.
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Figure 4. SEM-EDS images of Ca-SA (a) and S.P@Ca-SA (c) and digital images of Ca-SA (b) and S.P@Ca-SA (d).
Figure 4. SEM-EDS images of Ca-SA (a) and S.P@Ca-SA (c) and digital images of Ca-SA (b) and S.P@Ca-SA (d).
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Figure 5. (a) FTIR of Ca-SA and S.P@Ca-SA. (b) XPS spectra of S.P@Ca-SA before and after adsorption.
Figure 5. (a) FTIR of Ca-SA and S.P@Ca-SA. (b) XPS spectra of S.P@Ca-SA before and after adsorption.
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Figure 6. XPS spectrum of (a) Pb 4f, (b) C 1s, (c) N 1s and (d) O 1s of S.P@Ca-SA before and after reaction.
Figure 6. XPS spectrum of (a) Pb 4f, (b) C 1s, (c) N 1s and (d) O 1s of S.P@Ca-SA before and after reaction.
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Figure 7. Adsorption of Pb(II) on S.P@Ca-SA as affected by aqueous pH.
Figure 7. Adsorption of Pb(II) on S.P@Ca-SA as affected by aqueous pH.
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Figure 8. (a) Adsorption isotherm of Pb(Ⅱ) onto the S.P@Ca-SA, and (b) Pb(Ⅱ) adsorption kinetics fitted by pseudo-first-order and pseudo-second-order models onto the S.P@Ca-SA.
Figure 8. (a) Adsorption isotherm of Pb(Ⅱ) onto the S.P@Ca-SA, and (b) Pb(Ⅱ) adsorption kinetics fitted by pseudo-first-order and pseudo-second-order models onto the S.P@Ca-SA.
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Figure 9. Regeneration studies of S.P@Ca-SA for Pb(II) over five cycles.
Figure 9. Regeneration studies of S.P@Ca-SA for Pb(II) over five cycles.
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Figure 10. Removal capacity of Ca-SA and S.P@Ca-SA for Pb(Ⅱ), Cu(Ⅱ), Zn(Ⅱ), and Cd(Ⅱ) ions.
Figure 10. Removal capacity of Ca-SA and S.P@Ca-SA for Pb(Ⅱ), Cu(Ⅱ), Zn(Ⅱ), and Cd(Ⅱ) ions.
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Table
Table 1. Pb removal capacities of various species of microalgae biomass reported in the literature [33].
Table 1. Pb removal capacities of various species of microalgae biomass reported in the literature [33].
SpeciesInitial Metal Concentration (mg/L)Type of WastewaterRemoval Capacity (mg/g)
Chaetoceros sp. 20Synthetic46.94
Chlorella sp. 50Synthetic20.95
Spirogyra500Real94.34
Cyanothece sp. 500Synthetic28.57
Phormidium sp. 10Synthetic5.15
Rhizoclonium hookeri1000Synthetic81.7
Spirulina platensis100Synthetic68.0
Table
Table 2. Equilibrium isotherm model parameters obtained from model fitting to experimental data.
Table 2. Equilibrium isotherm model parameters obtained from model fitting to experimental data.
Adsorbent Dose
(g/L)		Freundlich Model
KF
(L/g)		1/nR2 χ 2 SSE
19.480.270.980.498.42
54.320.290.961.376.33
102.990.400.990.902.51
Adsorbent Dose
(g/L)		Langmuir Model
Qm
(mg/g)		KL
(L/mg)		R2 χ 2 SSE
127.70.430.815.6429.3
513.20.250.981.834.61
1010.80.280.9847.44.93
Table
Table 3. Kinetic model parameters obtained from model fitting to experimental data.
Table 3. Kinetic model parameters obtained from model fitting to experimental data.
Adsorbent Dose
(g/L)		Pseudo First-Order Model
qe
(mg/g)		k1
(1/h)		R2 χ 2 SSE
175.51.030.923.4837.2
521.40.870.901.7911.7
1011.41.250.841.534.07
Adsorbent Dose
(g/L)		Pseudo Second-Order Model
qe
(mg/g)		k2
(g/mg/h)		R2 χ 2 SSE
180.30.010.990.5613.3
522.80.060.970.365.24
1011.60.390.890.252.88
Table
Table 4. Pb removal capacities of various biomass-based adsorbents reported in the literature.
Table 4. Pb removal capacities of various biomass-based adsorbents reported in the literature.
AdsorbentRemoval Capacity (mg/g)Reference
Lignin microspheres33.9[51]
Lignin-chitin hybrid material75.7[52]
Aminated epoxy-lignin72.4[53]
Bi-functionlized lignin53.8[54]
1, 2, 4-triazole modified lignin42[55]
Chitosan-vanillin derivatives of chelating polymers23.3[56]
S.P@Ca-SA87.9This study
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Purev, O.; Park, C.; Kim, H.; Myung, E.; Choi, N.; Cho, K. Spirulina platensis Immobilized Alginate Beads for Removal of Pb(II) from Aqueous Solutions. Int. J. Environ. Res. Public Health 2023, 20, 1106. https://doi.org/10.3390/ijerph20021106

AMA Style

Purev O, Park C, Kim H, Myung E, Choi N, Cho K. Spirulina platensis Immobilized Alginate Beads for Removal of Pb(II) from Aqueous Solutions. International Journal of Environmental Research and Public Health. 2023; 20(2):1106. https://doi.org/10.3390/ijerph20021106

Chicago/Turabian Style

Purev, Oyunbileg, Chulhyun Park, Hyunsoo Kim, Eunji Myung, Nagchoul Choi, and Kanghee Cho. 2023. "Spirulina platensis Immobilized Alginate Beads for Removal of Pb(II) from Aqueous Solutions" International Journal of Environmental Research and Public Health 20, no. 2: 1106. https://doi.org/10.3390/ijerph20021106

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