DOI:
10.1039/C5RA22600G
(Paper)
RSC Adv., 2016,
6, 14705-14711
Albumin-functionalized magnetic nanoparticles as an efficient sorbent for removal of Pb(II), Cd(II), Cu(II) and Cr(VI) ions from aqueous solutions
Received
28th October 2015
, Accepted 8th January 2016
First published on 13th January 2016
Abstract
Functionalized magnetic nanoparticles are increasingly attracting interest as a new and efficient sorbent for metallic contaminant elimination in environmental samples. Albumin modified magnetic nanoparticles (AMMNPs) were synthesized and characterized. This sorbent was used for removal of cationic and anionic species from the aqueous solutions. The sorbent showed a high adsorption capacity and short equilibrium time for Pb2+, Cu2+, Cd2+ and CrO42− ions removal from aqueous solutions. The effects of different parameters on the adsorption processes were investigated and isotherm curves were constructed. This study showed that AMMNPs are a proper adsorbent for the removal of the studied hazardous ions and can also be used as an efficient sorption material for preconcentration of the studied ions in trace analyses. The adsorption process was very fast and adsorbent performance was not affected clearly by the presence of other ionic species.
1. Introduction
Metallic pollutants are a serious threat to the environment, food chain and human health. Their biological behavior and toxic effects can cause many problems in the areas of agriculture and health and to the environment all over the world.1 It is therefore obvious that the study of metallic pollutant removal is necessary. There have been reported relatively large numbers of scientific studies for eliminating metal ions from water and wastewaters, including chemical precipitation,2 reverse osmosis,3 electrochemical reduction,4 ion exchange5 and adsorption.6
Among these methods, the use of adsorbents is very attractive because of their low cost and high efficiency. The common adsorbents are activated carbon,7 carbon nanotubes,8 charcoal,9 clays,10 zeolites,11 composite materials,12,13 biomass,13 nanomaterials14 and polymeric materials.15 The efficiency of an adsorbent depends on the specific surface area, number of adsorption sites and chemical stability.16
Nanomaterials have unique features, and because of their small size, they possess a high surface area to volume ratio.17 Magnetic nanoparticles (MNPs) are a prevalent type of sorbent, which are widely used all over the world. These particles have a low cost, show sufficient magnetic properties and can be easily modified without altering their properties significantly. These features make them adsorbents with a great number of active sites and high efficiency. The most important advantage of using magnetic nanoparticles is manipulation simplicity.18
Albumin is the most abundant protein in mammalian blood serum, which is involved in the transport of hormones, fatty acids, small molecules and metal ions.19 This protein can adsorb metals because of their structural functional groups. It is expected that HSA shows a strong affinity towards transition metal ions because of the existence of amino acid residues such as histidine and cysteine.20 These amino acids have S and N atoms, which bind effectively with transition metal ions. In fact, a physical adsorption can also exist because of abovementioned functional groups in the albumin structure. In this study, our aim is the synthesis and characterization of the albumin modified magnetic nanoparticles (AMMNPs) and investigation of their ability to removal of the selected metal ions from aqueous solutions. We also intend to introduce AMMNPs as an effective and reliable adsorbent for preconcentration of the selected ions in trace analyses.
2. Materials and method
2.1. Materials
Hydrochloric acid, ethanol, sodium hydroxide, ferric chloride hexahydrate, ferrous chloride tetrahydrate, 25% ammonia solution, potassium dichromate, lead(II) nitrate, cadmium nitrate, and copper(II) nitrate were obtained from Merck (Germany). Amino propyl triethoxysilane (APTES) and tetra ethyl orthosilicate (TEOS) were purchased from Fluka (USA). A 25% human serum albumin (HSA) solution was prepared from Kedrion (Lukka, Italy).
2.2. Apparatus
Characterization of the sorbents was performed using a Jasco, 6300 Fourier transform infrared spectrometer (FT-IR) in the range of 400–4000 cm−1. The superparamagnetic properties of the magnetic particles were verified by the magnetization curve measured by the Alternating Gradient Force Magnetometer (AGFM). A Vega Tescan-LMU (Brno, Kohoutovice, Czech Republic) scanning electron microscope (SEM) was used to study the nanoparticles surface. The atomic absorption spectrometer was a Shimadzu, AA-670 and it was used with an air/acetylene flame for measuring all the investigated cations.
2.3. Synthesis of silica coated magnetic nanoparticles
The silica coated magnetite nanoparticles were obtained by a co-precipitation method.21 In a conventional synthesis, 12.3 g of FeCl3·6H2O and 4.60 g of FeCl2·4H2O were dissolved in 800 mL deionized water in a round bottomed flask under nitrogen with mechanical stirring at 80 °C. Then, 20% of 30 mL NH3 solution was added dropwise into the solution and a color change was observed immediately. The product was rinsed with deionized water twice. The resulting nanoparticles were dispersed in deionized water and then appropriate amounts of TEOS were added, and the pH value was increased to 12–13 by adding 25% ammonia solution while it was stirred with a mechanical stirrer. The suspension was sonicated at 85 °C for 30 min, and the pH was reduced to 6 by HCl. The synthesized product was washed three times with deionized water, and a brown precipitate was achieved.
2.4. APTES functionalized silica coated MNPs
The surface of the silica coated magnetic nanoparticles was activated by using APTES and glutaraldehyde for HSA immobilization.21 4 g of the magnetic nanoparticles prepared above was dispersed into 250 mL methanol in a flask; then 7 mL APTES and 3 mL deionized water was added dropwise to this solution and kept in an ultrasonic for 30 min. Subsequently, 150 mL glycerol was mixed into the solution by mechanical stirring at 90 °C for 3 h. The products were collected by a permanent magnet and washed with methanol–water (50–50) solution three times. Then, 20 mL glutaraldehyde and 0.1 M phosphate buffer were added to the flask followed by sonication for 6 h for surface activation. The collected nanoparticles were washed several times with deionized water to remove excess glutaraldehyde and other remaining reagents.
2.5. Preparation of MNP functionalized with albumin
HSA immobilized magnetic nanoparticles were synthesized with the process as follows: 10 mL HSA solution was added to the phosphate buffer solution in a round-bottomed flask. Then, 5 g of treated magnetic nanoparticles was immersed in this solution; after mixing for 4 h under vigorous stirring, the resultant materials were separated by a magnet and washed several times with deionized water.
2.6. Adsorption experiments
All the adsorption experiments were carried out using a batch adsorption technique. To study adsorption phenomena, a microcentrifuge tube was used and the volume of solution fixed at 1 mL. To perform the experiment the metal solutions were prepared and transferred to microcentrifuge and AMMNPs were added to the solution. To investigate the pH effect, the pH was varied by 0.1 M HCl and NaOH with the temperature maintained at 25 °C. pH measurements were carried out in 10 mL solutions. In all the adsorption experiments, the sorbent dose and ion concentration were fixed at 0.0014 g mL−1 and 10 ppm, respectively.
AMMNPs were dispersed in solution by an ultrasonic bath for 10 min and adsorbent separation was carried out using a magnet. All the experiments were repeated twice.
An atomic absorption spectrophotometer was used to find the residual ion concentrations. To evaluation the effect of each parameter the studied parameters were fixed at the previously mentioned level and others were varied. To compare the adsorption efficiency of adsorbent in different conditions the removal percentage and adsorbed concentration per mass of adsorbent, q (mg g−1) were calculated as follows:22
where
V is the solution volume,
W is the mass of the adsorbent, and
Cini and
Ce are initial and equilibrium concentration of the cations, respectively.
The isotherms were constructed using Langmuir and Freundlich models. The Langmuir adsorption model assumes that the all adsorption sites of the adsorbent have equal energy, and the adsorbent surface is homogeneous. The linear form of the Langmuir adsorption model is given as follows:
|
 | (1) |
where
qe is the adsorption capacity of metal ions (mg g
−1),
Ce is the equilibrium concentration (mg L
−1) in the liquid phase,
qm is the maximum adsorption capacity (mg g
−1) and
b is the Langmuir constant (L mg
−1).
The dimensionless quantity (f) was calculated to express the adsorption efficiency of the process. The equation is as follows:
|
 | (2) |
where
C0 and
b are the initial concentration of ion and Langmuir isotherm constant, respectively. A
f-value lower than 1.0 indicates a higher tendency for adsorption.
23
The Freundlich model illustrates the adsorption phenomena based on the heterogeneity of the sorbent surface. In addition, this model considers multilayer adsorption as follows:
where
qe is the amount adsorbed (mg g
−1),
Ce is the equilibrium concentration (mg L
−1), and
Kf and 1/
n are related to the adsorbent capacity and the sorption intensity of the adsorbent, respectively.
Eqn (3) can be linearized as follows:
|
 | (4) |
3. Results and discussion
3.1. Characterization of MNP
3.1.2 Magnetic properties of MNPs. Isolation of magnetic nanoparticles sorbents from solutions is easily possible using a magnet, therefore the magnetization power of sorbents is essential. The magnetic properties of modified MNPs were determined and compared with the original nanoparticles. Fig. 2 shows the magnetization curve as a function of perpendicular magnetic field for AMMNPs at room temperature.The S shaped behavior indicates the super paramagnetic feature of the adsorbents. In the absence of a magnetic field the magnetization value was zero, and the saturation magnetization was at 18.51 emu g−1, this observation implies that these surface modified MNPs have strong magnetic properties and can be isolated conveniently from a matrix solution using an external magnet.28
3.1.3 SEM images. Fig. 3 shows SEM micrographs of (a) Fe MNPs, (b) amino modified silica coated MNPs and (c) AMMNPs. It could be observed that the coating of the sorbents did not change the uniform size distribution. The adsorbents have a spherical and quasi spherical shape and a relatively high surface area. The average size of the MNPs was about 30 nm and after coating and functionalization, the average size was increased to about 85 nm. In addition, Fig. 3b and c clearly shows that the silica coated MNPs functionalization does not result in the change of morphology, but the aggregation of the noncoated MNPs is more evident than that of coated forms.
 |
| Fig. 3 SEM micrograph of MNPs (a), amino modified silica coated MNPs (b) and AMMNPs (c). | |
3.2. Influence of experimental conditions on the adsorption process
3.2.1 Effect of pH. One of the most effective factors of the adsorption phenomena is pH. Fig. 4 shows the significant role of pH on Cd2+, Cu2+, and Cr(VI) adsorption on the AMMNPs. As reported in the literature, the HSA isoelectric point (pI) was equal to 4.7. The results showed a distinct change in removal percentages at this pH value. The variations arose because of this fact that, potassium dichromate makes several forms of chromium ions in aqueous solutions. These ions, depending on pH of the solution, are chromate (CrO42−), dichromate (Cr2O72−) and hydrogen chromate (HCrO4−).29 In acidic media, the negatively charged HCrO4− is the dominant specie. The surface functional groups of the adsorbent, such as NH2 and OH, can be protonated and create positively charged NH3+and OH2+ species and therefore can serve as active sites for electrostatic adsorption of Cr(VI) ions. When pH becomes more than 5, the sorption decreased greatly because of the electrostatic repulsion among the COO− groups and CrO42− and Cr2O72− anions. In addition, in alkaline solution OH− competes with chromate and dichromate ions to diffuse into the surface of sorbent. Therefore, the adsorption of these ions was decreased at pH > 5.
 |
| Fig. 4 Effect of pH on removal percentage of Cd2+, Cu2+, Cr(VI) and Pb2+. | |
Cd2+ ions were strongly adsorbed in the pH range of 5–7, the surface of the sorbent was positively charged at pH < 5 and the repulsive electrostatic forces became possible between charged species of Cd2+ and the charged MNPs surface, especially protonated carboxylic groups; therefore, the ability as a sorbent for Cd2+ adsorption was decreased, whereas the decrease in adsorption at higher pH may be attributed to the hydrolysis of cadmium ions and also because of competition with hydroxyl groups with the ions. The active sites for copper binding to albumin are N-terminal amines. As shown in Fig. 4, the maximum Cu2+ adsorption occurred at low pH (pH = 4) and the removal percentage was decreased concurrently with pH enhancement. When pH was more than 5, the adsorption efficiency was decreased dramatically. It was expected that increasing the pH would cause an increased adsorption because of the negative charge on N atoms and electrostatic interactions. These results do not imply these facts and this behavior may have been due to the fact that copper precipitation has occurred.30 Varying the pH did not show a distinct change for removal efficiency of Pb2+.
3.2.2 Effect of adsorbent dose. To find the proper amounts in all experiments, different amounts of AMMNPs were tested. The effect of adsorbent dose of AMMNPs on the cadmium uptake is shown in Fig. 5. It was evident from this figure that adsorption efficiency increased very rapidly when the sorbent dose was increased up to 0.0014 g mL−1.
 |
| Fig. 5 Effect of adsorbent dose on adsorption capacity. | |
Adsorbent dosage provides more active site and more contact surface area for metal ion adsorption. In contrast, when adsorbent dosage was above 0.0014 g mL−1, the removal percentage variation was slow and therefore adsorption capacity decreased. These behaviors may have been due to adsorption site aggregation that can cause in a decrease in total adsorbent surface area.
3.2.3 Effect of temperature. Fig. 6 presents the effect of temperature on the adsorption behavior of the adsorbent. The removal of Cd2+ and Cu2+ ions from aqueous solutions decreased dramatically above of 30 centigrade. This can be explained by the fact that in higher temperatures, some chemical bonds will break, and therefore HSA to be denatured and finally it caused a reduction in the available active sites for metal ions.
 |
| Fig. 6 Effect of temperature on the removal of Cd2+, Cu2+, Cr(VI) and Pb2+. | |
The AMMNPs have a higher chromium adsorption capacity above of 30 °C, which reveals the endothermic nature of the adsorption phenomenon. In the case of Pb2+, the temperature did not show a sensible adsorption effect.
3.2.4 Effect of ultrasonic time. One of the effective factors for adsorption efficiency is contact time. The effect of different ultrasonic times to find the optimum time was studied. As shown in Fig. 7 for Pb2+, Cd2+ and Cu2+, a rapid kinetic adsorption was observed and the adsorption equilibrium time was at about 8 min. At longer times the removal percentage did not change distinctly.
 |
| Fig. 7 The relationship between ultrasonic time and percent removal at 25 °C for Cd2+, Cu2+, Cr(VI) and Pb2+. | |
The results for Cr(VI) adsorption show different behavior; the optimal time for Cr(VI) adsorption was 4–5 min. At longer contact times the removal efficiency was decreased. The reason of this phenomenon maybe was the rate of desorption of chromium ions. At times longer than 8 min, the chromium ions have enough time for desorption and ion exchange with other ions can be an important factor for decreasing the adsorption efficiency.
3.2.5 Study of interferences. The performance of an adsorbent for industrial and analytical applications needs to be investigated in the presence of interferences. For this purpose, the analyte adsorption in the solutions containing of 1000 ppm NaCl and MgSO4 were investigated. The obtained results showed that Cu2+ and Cr(VI) adsorption were affected due to the presence of other ions and the adsorption amounts were decreased to below 3.6 mg g−1 and 3.2 mg g−1, respectively, whereas removal percentages were about 51% and 46%. Conversely, Pb2+ and Cd2+ ion adsorption in the presence of co-existing ions was high; the removal percentage for Pb2+ was 94.28% and for Cd2+ it was about 88.57%. This behavior can be attributed to the fact that interfering ions, such as Mg2+ and Na+, occupied available sites on the adsorbent and therefore the Cu2+ and Cr(VI) ions could not reach to active sites on the surface of adsorbent, while it seems that the active sites for Cd2+ and Pb2+ ion adsorption were different than the active sites for interfering ions.
3.3. Adsorption isotherms
Langmuir and Freundlich isotherm models were examined to choose the best fitting one to the obtained experimental data and to represent the mechanism of adsorption.
The results in the Tables 1 and 2 show that the data could be fitted better to the Langmuir model than the other isotherm (Fig. 8). The latter fact suggests the adsorption of ions on the surface formed a monolayer. The abovementioned results suggest strongly that the adsorption of metal ions on AMMNs is a chemical type.
Table 1 Langmuir parameters
Adsorbed ion |
Regression equation |
R2 |
qmax (mg g−1) |
b (L mg−1) |
Cd2+ |
y = 0.102x + 0.016 |
0.993 |
9.803 |
6.375 |
Cu2+ |
y = 0.084x + 0.041 |
0.998 |
11.904 |
2.048 |
Cr(VI) |
y = 0.062x + 0.104 |
0.986 |
16.129 |
0.596 |
Pb2+ |
y = 0.066x + 0.013 |
0.995 |
15.151 |
5.077 |
Table 2 Freundlich model parameters
Ion |
Kf (mg g−1) |
n (L g−1) |
R2 |
Cd2+ |
6.053 |
6.289 |
0.986 |
Cu2+ |
2.392 |
4.931 |
0.972 |
Cr(VI) |
5.308 |
2.840 |
0.767 |
Pb2+ |
13.77 |
2.762 |
0.902 |
 |
| Fig. 8 Equilibrium Langmuir (a) and Freundlich (b) isotherms for Cd2+, Cu2+, Cr(VI) and Pb2+ ions adsorption on the AMMNPs at 25 °C. | |
3.4. Competitive adsorption experiment
To study the effect of other ions on the analyte adsorption, binary solutions were examined. In each experiment, the analyte concentration was constant, whereas the concentration of the other ion was changed from 10 ppm to 30 ppm. The relationship between the removal percentage and the initial concentration of the competitor ion was investigated. The results demonstrated that Cd2+, Cr(VI) and Cu2+ can share active sites and therefore these ions compete with each other to reach the active sites. Oxygen ligands and histidine ligands prepare active sites in HSA. Sadler and Viles demonstrated that Cu2+ had a higher affinity than Cd2+ for their active sites.31 These results are consistent with our observations. The removal percentage for Cu2+ in the presence of Cd2+ was decreased but this effect was not effective compared with resulting decrease of Cd2+ removal in the presence of Cu2+. In addition, the change of concentration of competitor ions caused a variation of removal percentage that can be attributed to changes of ionic strength because of the presence of interfering ions.
3.5. Comparison with other adsorbents
To evaluate the efficiency of AMMNPs a comparison with various adsorbents was made for Cr(VI) removal (Table 3). For better assessment, four parameters were compared. Table 3 shows that AMMNPs needed the lowest time for chromium ion removal. In addition, the adsorbent dose of AMMNPs was 1.4 mg mL−1, which was lower than other sorbents. This feature caused the water treatment process to become economical. The most important parameter for comparing adsorbents is the maximum adsorption capacity (qmax), and the table shows that AMMNs and surface modified sand has the greatest qmax value.
Table 3 Comparison between various adsorbents used for metal ion removal
Adsorbent |
Analyte |
Contact time (min) |
Initial concentration (mg L−1) |
Maximum adsorption capacity (mg g−1) |
Adsorbent dose (mg mL−1) |
Ref. |
Bare magnetic nanoparticles |
Cr(VI) |
10 |
5–15 |
3.55 |
4 |
32 |
Surface modified sand |
Cr(VI) |
1440 |
20 |
16.95 |
10 |
33 |
Fe@Fe2O3 core–shell nanowires |
Cr(VI) |
— |
8 |
7.78 |
1 |
34 |
Elaeagnus tree leaves |
Cr(VI) |
100 |
10–50 |
10.94 |
10 |
35 |
Amino starch |
Cr(VI) |
120 |
— |
12.50 |
— |
36 |
Chitosan coated resin |
Cr(VI) |
1440 |
0.4 |
0.03 |
— |
37 |
Amorphous and mesoporous silica |
Cr(VI) |
60 |
100 |
3.50 |
6.6 |
38 |
Silica gelatin composite |
Cr(VI) |
160 (h) |
260 |
9.41 |
2 |
39 |
Porous silica |
Cr(VI) |
1440 |
5.2 |
35.51 |
10.4 |
40 |
HSA |
Cr(VI) |
8 |
10 |
16.10 |
1.4 |
This work |
3.6. Conclusions
In this study, preparation and modification of magnetic nanoparticles using albumin were performed and their characterizations were obtained. The ability of AMMNPs toward Cr(VI), Cd2+, Pb2+ and Cu2+ ion adsorption was investigated. The obtained results showed a rapid, effective and economically favored adsorption method for the removal of selected ions. The variation of parameters did not show a detrimental effect on Pb2+ adsorption behavior. Because the results presented equally for both cationic and anionic species, it is concluded that the important feature for AMMNPs is simultaneous adsorption of both anions and cations. This property is because of effective functional groups in the albumin structure that were modified on the surface of MNPs. Displaying immobilization of albumin to the surface of MNPs is of significance for magnetic applications in the removal of toxic metal ions from water and wastewaters. Moreover, this adsorbent, because of its high efficiency can be a good candidate for preconcentration of trace levels of the investigated ions prior their determination by conventional analytical methods.
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