Figures
Abstract
A fundamental investigation of the biosorption of Cd2+ from aqueous solution by the edible seaweed Sargassum fusiforme was performed under batch conditions. The influences of experimental parameters, such as the initial pH, sorption time, temperature, and initial Cd2+ concentration, on Cd2+ uptake by S. fusiforme were evaluated. The results indicated that the biosorption of Cd2+ depended on the initial Cd2+ concentration, as well as the pH. The uptake of Cd2+ could be described by the Langmuir isotherm model, and both the Langmuir biosorption equilibrium constant and the maximum biosorption capacity of the monolayer decreased with increasing temperature, thereby confirming the exothermic character of the sorption process. The biosorption kinetics follows the pseudo-second-order kinetic model, and intraparticle diffusion is the sole rate-limiting step for the entire biosorption period. These fundamental equilibrium and kinetic results can support further studies to the removal of cadmium from S. fusiforme harvested from cadmium-polluted waters.
Citation: Zou H-X, Li N, Wang L-H, Yu P, Yan X-F (2014) Equilibrium and Kinetic Studies of Cd2+ Biosorption by the Brown Algae Sargassum fusiforme. PLoS ONE 9(4): e95242. https://doi.org/10.1371/journal.pone.0095242
Editor: Tilmann Harder, University of New South Wales, Australia
Received: January 28, 2014; Accepted: March 24, 2014; Published: April 15, 2014
Copyright: © 2014 Zou et al. This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.
Funding: This material is based upon work funded by China Natural Science Foundation (31270541)(http://www.nsfc.gov.cn/publish/portal0/default.htm), Zhejiang Provincial Natural Science Foundation of China (LQ13C030005)(http://www.zjnsf.gov.cn/), Plan for Qianjiang Talent of Zhejiang (QJD1202014) and Program for Wenzhou Science & Technology Innovative Research Team of China (C20120007-08). The funders had no role in study design, data collection and analysis, decision to publish, or preparation of the manuscript.
Competing interests: The authors have declared that no competing interests exist.
Introduction
Cadmium is one of the most toxic metals that affects the environment and human beings. Mining and metallurgy of cadmium, cadmium electroplating processes, battery and accumulator manufacturing, and pigments and ceramics industries produce wastewater that contains undesirable amounts of Cd2+ ions [1]. Moreover, cadmium can accumulate in the tissue of plants growing in industrially polluted areas, and this metal can be transferred to humans through food chains [2].
The brown seaweed Sargassum fusiforme (Sargassaceae, Phaephyceae) is among the most mineral-rich algae that is high in calcium, iodine, and magnesium, and is commonly found along the coastlines of China, Japan, and Korea [3]. In ancient Asia, this seaweed was not only used as a traditional medicine but was also enjoyed as a popular food for its nutty flavor. This alga, in great demand, is also cultivated in these counties, especially in China, where the cultivation area was 2.6% (2,482 ha) of the entire coastal area for the commercial cultivation of seaweeds with a total production of 32,000 tonnes (freshweight) [4].
Huerta-Díaz et al. [5] determined that Sargassum can accumulate large amounts of divalent metals. In this process of biosorption, the cell wall plays an important role in metal binding because it contains high concentrations of polysaccharides [6], including alginate, which is the main polysaccharide responsible for the biosorption of metals in Sargassum [7], [8].
The biosorption of cadmium ions by different living and dead types of algae has been extensively studied [9]–[14]. Numerous reports have recently suggested approaches that use living and nonliving algae for accumulating or removing heavy metals from aqueous solutions. However, neither the equilibrium nor the kinetic modeling of Cd2+ biosorption by dried S. fusiforme has been investigated.
Thus, in this work, we studied the biosorption of cadmium ions by S. fusiforme by investigating the influences of different experimental parameters on cadmium uptake, including the initial Cd2+ concentration, the initial pH, the sorption time, and the temperature. The experimental data were correlated with different kinetic and biosorption models, and the corresponding parameters and their temperature dependence were determined. These parameters provide fundamental information for use in further studies to remove cadmium ions from S. fusiforme harvested from cadmium-polluted waters.
Materials and Methods
Preparation of S. fusiforme
S. fusiforme samples were collected from the Northeastern coast of Wenzhou, China (28.0°N, 121.2°E) in October 2012. This location is not privately-owned or protected in any way, thus no specific permissions were required, and the field studies did not involve endangered or protected species. This sample was washed extensively with distilled water to remove particulate material from its surface, oven-dried at 333 K for 24 h, placed in desiccators, and allowed to cool to room temperature.
To remove divalent ions present in this native S. fusiforme sample and replace them with sodium ions (which can be easily displaced by metal ions) [5], [6], 50 g of dried S. fusiforme sample was treated with 0.1 mol L−1 HCl (500 mL) and then 0.1 mol L−1 NaOH (500 mL) for 1 h under slow stirring. The sample was then washed several times with deionized water until the pH of the rinse water was less than 10 [15]; this S. fusiforme sample was dried again at 333 K for 24 h.
Standard sampling techniques were applied to ensure the homogeneity of samples used in these experiments. The dried sample was chopped and sieved, and the 0.5–0.6 mm fraction was selected for use in the sorption tests.
Chemicals
All solutions were prepared from deionized water and an analytical grade salt of Cd(NO3)2·4H2O (Shanghai Aladdin Co., China). The solution pH was measured with a pH meter (METTLER TOLEDO, model Delta 320, China) and was adjusted to 5 with 0.1 mol L−1 HCl and/or 0.1 mol L−1 NaOH.
Biosorption experiments
Batch biosorption experiments were performed in 250 mL stoppered conical flasks that contained 0.500 g of S. fusiforme and 100 mL of Cd2+ standard solution. These test solutions were agitated in a 120 rpm controlled-temperature reciprocating shaker reciprocating shaker (SHA-B, China) at a constant temperature for 2 h. The influence of the initial solution pH (1–8), the contact time (2–120 min), and the initial Cd2+ concentration (30–300 mg L−1) were investigated. We conducted biosorption equilibrium experiments by combining 0.500 g S. fusiforme with 100 mL Cd2+ standard solution at different initial concentrations and at various temperatures (278 K, 288 K, 298 K, and 308 K). Kinetic studies were performed by mixing 0.500 g S. fusiforme with 300 mg L−1 Cd2+ solution in a series of 250 mL stoppered conical flasks. These flasks were removed at certain time intervals as shown in figures. After biosorption, the S. fusiforme was separated by centrifugation; the supernatant fluids were analyzed and the residual Cd2+ concentrations were measured using an atomic absorption spectrophotometer (Persee Tas 986, China) with a detection limit of 1.0 ppm at a wavelength of 228.8 nm. All samples were detected in duplicate. The accuracies for the Cd2+ analyses were achieved by comparing the measured concentrations to the added Cd2+ standards. The precisions and accuracies of the determination were estimated by replicating analysis (n = 5) of QC samples at three concentrations levels.
The amount of Cd2+ adsorbed at equilibrium, qe (mg g−1), i.e., the amount of Cd2+ adsorbed per unit mass of S. fusiforme at equilibrium (mg g−1), was calculated by:(1)where C0 is the initial concentration of Cd2+ (mg L−1), Ce is the equilibrium concentration of Cd2+ in solution (mg L−1), V is the volume of the solution (mL), and m is the mass of dry algae (g). Preliminary experiments had shown that cadmium biosorption losses on the flask walls and the filter paper were negligible.
Data analyses
Equilibrium biosorption isotherms provide fundamental information related to the design of biosorption systems. An isotherm indicates how adsorbate molecules are distributed between the liquid phase and the solid phase when the biosorption process reaches equilibrium [16]. In the present investigation, the biosorption data were analyzed using Langmuir and Freundlich isotherm models. The Langmuir isotherm model is based on the assumption that a monolayer adsorbs onto a homogeneous surface containing a finite number of biosorption sites with uniform strategies of biosorption and no transmigration of adsorbate on the plane of the surface [17]. The linear form of the Langmuir isotherm model is given by the following equation:(2)where Ce is the equilibrium concentration of Cd2+ in solution (mg L−1), qm is the maximum biosorption capacity of the monolayer (mg g−1), and KL is the Langmuir biosorption equilibrium constant related to the energy of biosorption (L mg−1). The values of qm and KL can be evaluated from a linear plot of Ce/qe as a function of Ce.
The Freundlich isotherm model is an empirical equation used to describe heterogeneous systems [18], and it is represented by the following linear equation: (3)where KF ((mg g−1) (mg−1 L)1/n) and 1/n are Freundlich constants related to adsorbent biosorption capacity and biosorption intensity, respectively. The KF and n values can be calculated from the intercept and the slope of a liner plot of log qe as a function of log Ce.
To analyze the biosorption kinetics of Cd2+, pseudo-first-order and pseudo-second-order kinetics models were applied in this study. The equation of the pseudo-first-order kinetics model can be written as:(4)where qe and qt are the amount of Cd2+ adsorbed (mg g−1) at equilibrium and at time t, k1 is the pseudo-first-order equilibrium rate constant (min−1), and t is the contact time (min). However, to adjust Eq. (4) to fit the experimental data, the value of qe must be pre-estimated through extrapolation of the experimental data to t ∝ ∞.
The pseudo-second-order kinetic rate equation is expressed as:(5)where k2 is the pseudo-second-order rate constant (g mg−1 min−1). A plot of t/qt versus t should be a straight line if pseudo-second-order kinetics are applicable, and qe and k2 can be determined from the slope and intercept of this plot, respectively.
Because the pseudo-first-order and pseudo-second-order kinetics models cannot identify the diffusion mechanism, the kinetic biosorption data were further evaluated using an intraparticle diffusion model. The intraparticle diffusion model, as expressed by Weber and Morris [19], can be described as:(6)where kid is the intraparticle diffusion rate constant (mg g−1 min−1/2) and C is the intercept.
Results and Discussion
Precisions and recoveries of the Cd2+ analyses
The linear regression result of absorbance against Cd2+ concentration detected by atomic adsorption spectrophotometer is , the correlation coefficient is 0.9997, where A is the absorbance of Cd2+, C is the concentration of Cd2+ (the linear range of Cd2+ is from 1 mg L−1 to 8 mg L−1). The precision and accuracy results are summarized in Table 1. The precision of the determination is described as relative standard deviation (RSD) among each assay. The accuracy is evaluated by the recovery values, which described as a percentage error of the measured concentrations vs. QC added concentrations. As can be seen from Table 1, the RSD values are lower than 0.6%, and the recovery values are among the range of 96.3–97.1%. So the determination shows desired precision and accuracy.
Effect of initial pH
The initial pH is one of the most important parameters controlling the biosorption of metal ions because it affects both the surface binding sites of the adsorbent and the ionization process of the metal ions [12]. In the present biosorption system, the effect of initial pH was evaluated within the range of 1.0–8.0 at a concentration of 300 mg L−1 of Cd2+. As shown in Fig. 1, the increase of Cd2+ biosorption efficiency with pH is made until to the optimum pH value is reached (pH 7). Solution pH is known to influence cell surface metal binding sites and metal chemistry in water. Hence, the biosorption of Cd2+ onto S. fusiforme is influenced primarily by the surface charge on the cell wall of the brown algae, which is influenced by the solution pH. At low pH levels, functional groups from cell walls were associated closely with the hydronium ions of H3O+ and restricted the approach of metal cations as a result of repulsive forces [20]. As the pH increased, more functional groups such as carboxyl, phosphate, imidazole and amino groups in the cell wall would be exposed, and their negative charges would subsequently attract metallic ions with positive charges that biosorb onto the cell surface [21]. At higher pH values (7.0–8.0), the surface of S. fusiforme may reach the zero-point charge, or isoelectric point, and thus not affect the Cd2+ biosorption [22]. So pH = 7 is the optimum value.
Effect of contact time
The effect of contact time on the biosorption of Cd2+ by S. fusiforme was investigated using a constant initial Cd2+ concentration of 300 mg L−1 at 298 K. As shown in Fig. 2, the biosorption of Cd2+ increases sharply during the first 25 min, increases more slowly up to 60 min, and then remains almost constant after 60 min. The initial rapid stages are attributed to the abundant availability of active binding sites on the cell wall of the S. fusiforme, and, with gradual occupancy of these sites, the biosorption becomes less efficient in the later stages [23]. Although the equilibrium time was 60 min for all the biosorbents used in this study, the contact time was fixed at 120 min for the remainder of the batch experiments to ensure that equilibrium was reached.
Effect of initial Cd2+ concentration
Figure 3 shows the effect of the initial Cd2+ concentration on the biosorption of Cd2+ by S. fusiforme and indicates that the biosorption capacities of S. fusiforme increased with the initial Cd2+ concentration. When the initial Cd2+ concentration was increased from 30 to 300 mg L−1 (298 K), the biosorption capacity of S. fusiforme increased from 16.2 to 33.1 mg g−1. Higher initial Cd2+ concentrations not only provide a larger driving force to overcome all mass transfer resistances of Cd2+ between the aqueous and solid phases but also result in a higher probability of collision between Cd2+ and binding sites from S. fusiforme surfaces [24].
Additionally, also in Fig. 3, the amount of Cd2+ adsorbed by S. fusiforme at equilibrium (qe) is decrease with the increase of the temperature. For example, at the initial Cd2+ concentration of 300 mg L−1, the value of qe is decreased from 18.15 mg g−1 to 12.92 mg g−1, which means that the process of Cd2+ sorption by Sargassum sp. is exothermic, as observed for other systems such as Cd2+-Sargassum sp. [24], Cd2+-Sargassum baccularia [25], and Cd2+-Sargassum fluitans [26]. Therefore, an increase in temperature is beneficial for removing Cd2+ from S. fusiforme.
Equilibrium study
The Langmuir isotherm plots and Freundlich isotherm plots for Cd2+ biosorption at different temperatures are shown in Fig. 4 and Fig. 5, their values are also listed in Table 2. As shown in Table 2, the values of n are all within the range of 1–10, further indicating that these biosorption processes are favorable under the previously described conditions [27].
In the present study, the correlation coefficient (R2) was used to confirm the best-fit isotherm for this biosorption system. The results are shown in Table 2. The Langmuir isotherm model appears to fit the isotherm data better than the Freundlich model because the correlation coefficients are higher for Langmuir's model. The fit of equilibrium data to the Langmuir model may indicate that the biosorption of Cd2+ onto S. fusiforme is monolayer biosorption. As also shown in Table 2, the values of the Langmuir constants qm and KL all decreased with increasing temperature, which suggests that both the biosorption capacity and the energy of biosorption tend to decrease with increasing temperature, thereby confirming the exothermic character of the sorption process.
Because KL is an equilibrium constant, its dependence on temperature can be used to estimate both the enthalpy change (ΔH) and the entropy change (ΔS) associated with the biosorption process.(7)
The plot of ln KL as a function of 1/T yielded a straight line from which a ΔH value equal to −8.1 kJ mol−1 and a ΔS value equal to −2.69 J mol−1 K−1 were calculated.
A comparison of the values of ΔH and ΔS shows that the negative enthalpy change compensates for a sufficient amount of the entropy loss that the Gibbs energy changes are less than zero. Therefore, the biosorption of Cd2+ by S. fusiforme is a spontaneous and enthalpically driven process.
Biosorption kinetics
Figure 6 and Fig. 7 present pseudo-first-order and pseudo-second-order kinetics plots for the biosorption of Cd2+ on S. fusiforme, respectively. The kinetics parameters determined by the two models and the corresponding correlation coefficients (R2) are listed in Table 3. In this study, on the basis of the higher R2 values, the pseudo-second-order kinetic model gives a better fit to the biosorption data than does the pseudo-first-order model. This result demonstrates that the rate-limiting step for biosorption may be chemical biosorption involving covalent forces through sharing or the exchange of electrons between S. fusiforme and Cd2+ metal ions. On the basis of physical biosorption capacity, the pseudo-first-order rate equation has been widely used to describe the biosorption of organic pollutants from wastewater [28]. However, the pseudo-second-order rate equation is based on chemical biosorption, especially chemical bonding among divalent metal ions and polar functional groups such as aldehydes, ketones, and acids on biomass [29]. In this study, algal acidic functional group is assumed to be responsible for the cation-biosorption capacity of S. fusiforme.
Biosorption always occurs through three consecutive steps [30]: (1) diffusion across the liquid film surrounding the adsorbent particles, i.e., external diffusion of Cd2+ toward S. fusiforme; (2) diffusion in the liquid contained in the pores and/or along the pore walls, which is so-called internal diffusion or intraparticle diffusion, i.e., the diffusion of Cd2+ at the rough cell surface of S. fusiforme; and (3) biosorption and desorption between the adsorbate and active sites, which includes a number of passive accumulation processes and may include biosorption, ion exchange, coordination, complexation, chelation, and microprecipitation.
According to the theory behind the intraparticle diffusion model, a plot of qt against t1/2 should yield a straight line if intraparticle diffusion is involved in the biosorption process; furthermore, if the straight line passes through the origin, then intraparticle diffusion is the sole rate-controlling step. Otherwise, the biosorption process may involve some other mechanisms in addition to intraparticle diffusion [31].
As shown in Fig. 8, the linear regression equation is Y = 0.2X−2.7×10−7, the coefficient for the intra-particle diffusion model is equal to 1, the small value of the intercept could be negligible, and thus intraparticle diffusion is the sole rate-limiting step.
Conclusions
In the present study, the biosorption of Cd2+ onto S. fusiforme could be described by the Langmuir biosorption model. Both the Langmuir biosorption equilibrium constant and the maximum biosorption capacity of the monolayer decreased with increasing temperature, thereby confirming the exothermic characteristic of the sorption process. In addition, the biosorption of Cd2+ by S. fusiforme is a spontaneous and enthalpically driven process.
The biosorption kinetics of Cd2+ onto S. fusiforme followed a pseudo-second-order kinetic model, which was based on chemical biosorption. Because the regression of the intra-particle diffusion model was fine, the diffusion rate is controlled solely by the intraparticle diffusion process.
Author Contributions
Conceived and designed the experiments: HXZ XFY. Performed the experiments: HXZ NL. Analyzed the data: HXZ LHW. Contributed reagents/materials/analysis tools: PY. Wrote the paper: HXZ XFY.
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