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Article

Modification of Magnetic Graphene Oxide by an Earth-Friendly Deep Eutectic Solvent to Preconcentrate Ultratrac Amounts of Pb(II) and Cd(II) in Legume Samples

by
Melika Hejazikhah
and
Parastoo Jamshidi
*
School of Chemistry, College of Science, University of Tehran, Tehran P.O. Box 14155-6455, Iran
*
Author to whom correspondence should be addressed.
Appl. Sci. 2023, 13(9), 5702; https://doi.org/10.3390/app13095702
Submission received: 13 December 2021 / Revised: 19 January 2022 / Accepted: 11 August 2022 / Published: 5 May 2023

Abstract

:
A novel magnetic solid-phase extraction adsorbent using deep eutectic solvent-coated magnetic graphene oxide (EgLiCl-mGO) was proposed for simultaneous preconcentration of Pb(II) and Cd(II). The nanocomposite was characterized by Fourier Transform Infrared Spectroscopy, X-ray diffractometry, and alternative gradient force magnetometer. Parameters that could affect the preconcentration recoveries of the target ions were investigated via the one-factor-at-a-time method. The optimum conditions are pH of 4 ± 0.5, EgLiCl-mGO amount of 1.0 × 10−2 g, adsorption time of 5 min, eluent of HNO3 (1 mL, 2 mol L−1), and desorption time of one minute. The swelling property of the adsorbent versus pH was studied. The linearity of the dynamic range for Pb(II) (5.0 × 10−6–4.0 × 10−4 g L−1) and Cd(II) (5.0 × 10−6–15 × 10−5 g L−1) was recorded. The limits of detection were Pb(II): 1.2 × 10−6 g L−1 and Cd(II): 47 × 10−8 g L−1. The preconcentration factor of 50 was calculated for both ions and the relative standard deviations were 1.27% for Pb(II) and 0.94% for Cd(II). Reusability, effect of interference ions, selectivity, isotherm adsorption, kinetic adsorption, and thermodynamic adsorption were established. The adsorbent was successful at preconcentrating the ions in legumes.

1. Introduction

Deep eutectic solvent (DES) has received attention in the recent years. DES is an emerging class of safe materials related to ionic liquid (IL), which has abnormally deep melting point depression at the eutectic mixture of specific hydrogen bond donors (HBDs) and acceptors (HBAs). DESs are divided into five categories depending on the method of preparation [1,2]. Type I is composed of a quaternary ammonium salt and a metal chloride, Type II is a mixture of a quaternary ammonium salt and a metal chloride hydrate, Type III is a mixture of a quaternary ammonium salt and an HBD, Type IV consists of a metal chloride hydrate and an HBD, and Type V consists of only nonionic, molecular HBAs and HBDs. All types of DESs have high thermal stability, low volatility, low vapor pressure, and tunable polarity. Their preparation does not need any extra solvent so no purification step is needed. Therefore, they are applicable substitutions for volatile organic compounds (VOCs), used widely throughout research and industry with the aim of environmental remediation, especially magnetic solid-phase extraction (MSPE) [3,4,5].
MSPE is a developed generation of solid-phase extraction, which uses magnetic or magnetically modified adsorbents to extract analytes with high efficiency. This tactic overcomes some weak points in solid-phase extraction such as decreasing the time of preconcentration, sample loading, and filtration or centrifugation steps [6,7,8]. Magnetic graphene oxide is an example of an MSPE adsorbent. Graphene oxide (GO) is a fascinating new class of two-dimensional carbon nanostructures. It has high surface area, good chemical stability, and strong thermal stability. GO contains hydroxyl, epoxide, carboxyl, and carbonyl functional groups; additionally, its hydrophilic property increases its negative charge and dispersibility in aqueous solution to form a stable suspension. GO has strong interaction with magnetic nanoparticles; accordingly, mGO can be a good candidate to be applied MSPE as an adsorbent. GO can be functionalized with organic components via π–π interaction to control selective adsorption of analyte(s) [9,10,11,12]. DES is an example, which can be a modifier, disperser, and fictionalizer for mGO.
Many scientists have used DES to improve the extraction or preconcentration methods. For example, a DES of ethylene glycol and ammonium-based salt functionalized carbon nanotube to adsorb methyl orange from aqueous solution [13]. Additionally, a novel DES was applied as a modifier for graphene and graphene oxide to remove chlorophenols [14]. In additional to organic materials, DES can be a qualified candidate to adsorb cations such as heavy metals, because it has active negative sites and can grab cations via electrostatic force [15].
In this study, magnetic graphene oxide modified with DES (EgLiCl-mGO) was applied as an efficient nanoadsorbent for preconcentrating Pb(II) and Cd(II) simultaneously in legume samples. Pb(II) and Cd(II) are toxic elements and their accumulative characters cause serious problems for humans, plants, and animals [16]. According to specific properties of EgLiCl-mGO, it could be a highly applicable adsorbent. mGO facilities the preconcentration procedure because graphene oxide has a high surface area and magnetic properties enable easy and fast separation of EgLiCl-mGO [7,17,18,19,20]. The presence of DES provided a wide surface area with functional groups, which has a synergistic effect on adsorption efficiency. More importantly, EgLiCl is inexpensive, biodegradable, nontoxic, and easy to prepare. For the evaluation of the effective variables on the preconcentration efficiency, the one-at-a-time method was employed and pH, adsorption time, adsorbent amount, desorption time, and kind of eluent were optimized. Analytical figures of merit, interference effect of various ions, reusability, swelling behavior, adsorption isotherm, adsorption kinetics, and adsorption thermodynamics were reported. Finally, the target analytes were analyzed in the four different legumes.

2. Materials and Methods

2.1. Apparatus

Absorbance quantifications of Pb(II) and Cd(II) were conducted using a flame atomic absorption spectrometer (FAAS; Younglin Aas 8020 (http://youngincm.com, Gyeonggi, South Korea)) with a deuterium background correction system and an air–acetylene burner. All pH adjustments were conducted with a digital pH meter (Metrohm—827 (www.metrohm-ag.com, Herisau, Switzerland)). The instrument has a glass combination electrode. The X-ray powder diffraction pattern (XRD; Philips—PW1730 (www.panalytical.com, Eindhoven, The Netherland)) was obtained under the Cu-Kα radiation (1.2 kW). 2θ ranged from 10° to 80°, scan step and step time were 0.05° and 1 s, respectively. An alternative gradient force magnetometer (AGFM; Meghnatis Daghigh Kavir Company (https://nano.kashanu.ac.ir, Kashan, Iran)) measured magnetic properties in an applied magnetic field sweeping between ±10,000 Oe. Fourier transform infrared spectra (FT-IR; ABB Bomem MB100 (http://new.abb.com, Zürich, Switzerland)) were recorded over the range 400–4000 cm−1.

2.2. Reagent and Solution

All the reagents were of analytical grade. The standards of Pb(II) and Cd(II) (1.0 × 10−3 g L−1) were prepared using their nitrates salts. Flake graphite, P2O5, H2SO4, K2S2O8, H2SO4, KMnO4, NaNO3, HCl, H2O2, FeCl3·6H2O, FeCl2·4H2O, NH4OH, ethylene glycol (Eg), and LiCl were procured from Merck Company (www.merck.de, Darmstadt, Germany). Ultra-high purity water from a Milli-Q system was used to prepare sample solutions.

2.3. Synthesis

Graphene oxide (GO) was prepared using the modified Hummer’s method. A mixture of flake graphite (4.0 × 10−3 g), H2SO4 (12 mL), and P2O5 (8 × 10−3 g) was magnetically stirred for 6 h and then filtered. Afterwards, H2SO4 (12 mL) and K2S2O8 (8.0 × 10−3 g) were added to the filtrate and was magnetically stirred for 6 h. The materials were cooled to room temperature, eluted by deionized water (300 mL), dried at room temperature, and then heated at 60 °C for 2 h. Pre-oxidized graphite powder (2.0 × 10−3 g), H2SO4 (92 mL), and KMnO4 (12 × 10−3 g) were stirred together in an ice bath. After 15 min, NaNO3 (2.0 × 10−3 g) was added to the materials and was stirred at room temperature for 2 h. Then deionized water (200 mL) was added and stirred for 15 min. H2O2 (30%, 10 mL) and distilled water (500 mL) were added. The materials were filtered and washed using HCl (10%) to reach the brown suspension, and then they were heated at 60 °C for 30 min. The cooled materials were sonicated in H2O2 (10%, 10 mL) for 5 min. The yellow-brown residual powder was washed with warm deionized water 3 times to remove the impurities. GO was dried at 60 °C [21,22].
Secondly, a magnetic carbonic nanocomposite was synthesized based on Massart’s method. Deionized water (100 mL), FeCl3·6H2O (2.5 g), FeCl2·4H2O (9.0 × 10−1 g), and GO (1.0 × 10−1 g) were sonicated for 15 min. Afterwards, under nitrogen atmosphere, NH4OH (25%, 15 mL) was dripped to fix the pH~11. After stirring for 12 h, mGO was magnetically gathered, eluted using distilled water, and dried at 80 °C [23].
Finally, Eg (5.0 × 10−2 g) and LiCl (5.0 × 10−2 g) were mixed together at 60 °C. A colorless liquid shows a successful synthesis of DES. mGO (5.0 × 10−2 g) was dispersed into the DES via one hour sonication. The final product (EgLiCl-mGO) was eluted using deionized water and then dried at 30 °C [24].

2.4. General Procedure

Pb(II) and Cd(II) (5.0 × 10−5 g L−1) were dissolved in deionized water (50 mL). EgLiCl-mGO (1.0 × 10−2 g) was added into the sample solution at the pH of 4 ± 0.5, followed by shaking for 5 min. EgLiCl-mGO was gathered magnetically. One-minute sonication in the presence of HNO3 (1 mL, 2 mol L−1) completed the process of preconcentration. Eluted ions were quantified by FAAS.

2.5. Sample Preparation

Four different legume samples including kidney bean, cowpea, pinto bean, and navy bean were procured from local stores in Tehran, Iran. The samples were cleaned with deionized water. They were dried to reach the stable weight, and then cooled to room temperature. The samples (1.0 × 10−1 g) were transferred into a Teflon vessel containing HNO3 (15 mL, 65%), and kept immersed for 48 h. The digestion heating steps are reported below: Firstly, the temperature was raised to 90 °C in 10 min and stayed for 5 min. Then, the temperature increased to 150 °C and remained for 10 min, followed by adding H2O2 (20 mL, 30%). Finally, the vessels were cooled down to room temperature. The solution in each vessel was transferred to a polyethylene volumetric flask and diluted to 100 mL. The pH of two separate 50 mL aliquots of digested samples was adjusted to 4 ± 0.5 using HNO3 and NH3 solutions. The general procedure was applied as mentioned in Section 2.4. Matrix spiking with standards of Pb(II) and Cd(II) (5.0 × 10−5) was employed to evaluate the effect of the matrix.

3. Results

3.1. Characterization

FT-IR spectra confirm that Eg-LiCl was loaded onto mGO completely (Figure 1). The FT-IR spectrum of mGO was drawn in the orange spectrum. The stretching O-H, carbonyl C=O, aromatic C=C, bending O-H, aromatic C-C, alkoxy C-O-C, stretching CH2, and carbonyl C=O bonds are identified according to the peaks of 3380, 1730, 1630, 1360, 1220, 1050, 2880, and 1730 cm−1, respectively. Peaks lower than 700 cm−1 characterize bonds of Fe–O [25]. The blue spectrum is related to EgLiCl-mGO. The bands of 3430 and 1640 cm−1 are associated O-H bonding. Alkane CH2 stretching, CH2 scissor, CH2 wagging, and CH2 twisting are characterized according to peaks around 2914, 1460, 1350, and 1258 cm−1, respectively. The sorption peaks of Li-O and Fe-O were seen at the wavelengths of 1300 and 700 cm−1, respectively [25]. Table S1 summarizes the data.
The X-ray diffraction (XRD) analysis of EgLiCl-mGO is patterned in Figure 2a, which has good agreement with JCPDS cards No. 01-075-0449, indicating magnetite Fe3O4 and JCPDS cards No. 01-079-1715 confirming the GO structure. Fe3O4 was characterized by peaks at 30.70, 35.97, 37.23, 43.74, 53. 94, 57.55, 63.32, and 67.14°. Additionally, peaks at 11.23, 21.64, 30.70, 35.97, 43.74, 53.94, 57.55, 63.32, and 75.08° are related to GO [26]. The process of loading EgLiCl onto mGO broadened the peaks of mGO. The crystal size of the total product was calculated using the Scherrer formula. It is about 6 nm.
The AGFM curve of EgLiCl-mGO is presented in Figure 2b. The amount of ±25 electromagnetic units (emu g−1) is helpful for the rapid gathering of the adsorbent in the sample solution [27]. The remanent magnetization is almost zero, confirming the superparamagnetic property and the presence of Fe3O4 nanoparticles.

3.2. Optimization of the Method

3.2.1. Effect of pH

Alkaline or acidic condition of samples plays a crucial part for the preconcentration of heavy metals by solid adsorbents because it has a direct effect on Pb(II) and Cd(II) ion retention on the negative sites of EgLiCl-mGO. It may be possible for the cations to form coordination compounds with oxygen groups via electrostatic force. Recovery of the investigated ions on the EgLiCl-mGO was found Pb(II): 99.1 and Cd(II): 98.4 in pH of 4 ± 0.5. Quantitative recovery values were found in the pH range of 2–9. After pH~5, recovery values of the preconcentrated ions decreased because heavy metal ions were hydrolyzed with formation of metal hydroxides. Therefore, pH~4 was applied as the optimized pH value for further experiments. Additionally, in highly acidic pH, the negative active sites will be occupied by H+ sooner than the target cations.

3.2.2. Effect of Adsorption Time

A certain period of time must pass to reach a complete adsorption. Accordingly, a fixed amount of EgLiCl-mGO was added to the sample solutions of Pb(II) and Cd(II) (50 mL, 5.0 × 10−5 g L−1) under the adsorption time, ranging from 1 to 30 min. The experiment results show that the performance of the method has increasing trend from 1 to 5 min, but after that there are slight differences in the recoveries. Therefore, the adsorption time of 5 min was selected for the next experiments.

3.2.3. Effect of Adsorbent Amount

An appropriate amount of adsorbent is an essential parameter in the MSPE method. On the one hand, this is effective for the usage amounts of materials; on the other hand, it provides sufficient active sites for adsorption of target analytes. In this context, the influence of EgLiCl-mGO amount on the simultaneous preconcentration efficiencies of Pb(II) and Cd(II) remained constant with the adsorbent amount ranging from 1.0 × 10−2 to 5.0 × 10−2 g. This indicates high affinity of EgLiCl-mGO toward these heavy metals. Therefore, 1.0 × 10−2 g was selected for the next step of optimization.

3.2.4. Effect of Eluent Type

The influence of the eluent type on the simultaneous preconcentration efficiency of Pb(II) and Cd(II) by EgLiCl-mGO was compared in the presence of two acids (Table 1). The highest analytical yields for the target analyte were observed using HNO3 (2 mol L−1). Afterwards, the volume influence of HNO3 on the extraction efficiency of the target analytes was studied in the range of 0.5–2 mL. The efficiency remained stable in all volumes. As one of the concerns in this article is using the minimum amounts of materials with the maximum performance, 1 mL was selected as the optimum volume of eluent.

3.2.5. Effect of Desorption Time

A completion of the desorption step depends on the desorption time. Insufficient desorption time does not let the eluent elute the adsorbed ions, resulting in poor analytical efficiency of the method. At the same time, it has a direct effect on the speed of preconcentration. Therefore, it is necessary to find the optimum desorption time. In the present study, the effect of desorption time on the method was studied in the range of 1–5 min and 1 min of shaking is sufficient for desorption of Pb(II) and Cd(II).

3.3. Swelling Behavior of EgLiCl-mGO

The swelling behavior of the adsorbent in different pH was investigated through the recording of the swelling ratio of EgLiCl-mGO in aqueous solution (50 mL) of Pb(II) (5.0 × 10−5 g L−1) and Cd(II) (5.0 × 10−5 g L−1). A certain mass of the adsorbent (1.0 × 10−2 g) was shaken into sample solution at different pH (ranging from 2 to 9) at 25 °C for 5 min. Then, the weights of the swelled adsorbent were recorded after decanting the water. The swelling ratio (SR) of the fibers was determined using Equation (1):
S R = W s W d W d
where Ws and Wd represent the weight of the wet adsorbent in water and that of dry adsorbent. Additionally, the pH effect of the sample solution on the swelling ratio was explored by recording SR in different pH ranging from 2 to 9 (Table 2). By increasing pH from 2 to 4, the swelling has an increasing trend but after that decreased significantly [28,29,30]. In all pH, EgLiCl-mGO adsorbed molecules of water via electrostatic interaction but in pH~4 the adsorption of Pb(II) and Cd(II) reached their maximum. The ion adsorption causes swelling of the adsorbent, illustrating the ability of EgLiCl-mGO to adsorb heavy metals.

3.4. Reusability of EgLiCl-mGO

First, EgLiCl-mGO (1.0 × 10−2 g) was shaken in an aqueous solution (50 mL) of Pb(II) (5.0 × 10−5 g L−1) and Cd(II) (5.0 × 10−5 g L−1) and the amounts of heavy metals ions in the eluent were determined using FAAS. Five consecutive cycles were completed according to the procedure in Section 2.4. The metal ion adsorption efficiencies decreased after the second cycle. The method is reusable for two times. This decrease is related to negative effect of eluent onto EgLiCl-mGO. Eluent impacts on EgLiCl and affect the interaction among the components.

3.5. Interference Effect of Various Ions and Selectivity of EgLiCl-mGO

The study of interreference effects on the suggested method is important, because the adsorption of Pb(II) and Cd(II) ions may be influenced by other cations and anions; consequently, the performance of the method decreases [31]. Adsorption of the target ions by EgLiCl-mGO was conducted in the presence of higher amounts of other ions with respect to their applications in real samples. The ±5% was considered as the maximum tolerance limit and values smaller than this amount were acceptable. Table 3 summarizes the data.
Under the optimum conditions, the selectivity of the method was studied. According to the data, the preconcentration efficiencies of Pb(II) and Cd(II) were 99% and 98%, respectively; however, the preconcentrating efficiencies of Cr(II), Cu(II), Mn(II), and Pd(II) were 32%, 85%, 17%, and 76%, respectively. This strength is related to selective interaction between target ions and specific active sites on the surface of EgLiCl-mGO. Pb(II) and Cd(II) have a smaller ionic radius so they have a greater charge density; consequently, they occupy the active sites of EgLiCl-mGO sooner and more strongly.

3.6. Sample Analysis

The accuracy of EgLiCl-mGO for simultaneous preconcentration of Pb(II) and Cd(II) in real samples was assessed through the spike method (5.0 × 10−5 g L−1). Four different legumes including kidney bean, cowpea, pinto bean, and navy bean were purchased from local stores in Tehran, Iran. The sample preparation is explained in the section of sample preparation in detail, followed by applying the optimum procedure regarding Section 2.4. The results are presented in Table 4. The recovery values for the analyte ions were satisfactorily reasonable in the range 95–101%. The amounts of Pb(II) and Cd(II) were quantified in both the spiked and unspiked samples regarding Equation (2). The determination of ions was conducted using a FAAS.
R % = C 1 C 2 C 3 × 100
where C1, C2, C3, and R% are spiked portion, unspiked portion, the amounts of the ions, and relative recovery, respectively.

3.7. Analytical Figures of Merit

Analytical figures of merit for the suggested procedure under the optimum conditions (Section 2.4) were determined from results of the analyses. The linear calibration equations for Pb(II) and Cd(II) were A = 0.0011C + 0.0047 (R2 of 0.988) and A = 0.0112C − 0.0172 (R2 of 0.998), respectively. Linearity of dynamic range (LDR) for Pb(II) (5.0 × 10−6–4.0 × 10−4 g L−1) and Cd(II) (5.0 × 10−6–15 × 10−5 g L−1) were recorded. In these equations, A is the absorbance of ions and C expresses as their concentrations in initial sample solutions. The limits of detection (LOD), expressed as 3Sb/m (Sb is blank standard deviation and m is slope of the calibration plot), were found as Pb(II) 1.2 × 10−6 g L−1 and Cd(II) 47 × 10−8 g L−1 for five measurements of the blank. The limits of quantification (LOQ) were Pb(II) 3.9 × 10−6 g L−1 and Cd(II) 1.5 × 10−6 g L−1. LOQ was defined as 3.33 LOD. The preconcentration factor (PF) of 50 was calculated as the concentrations of ions before and after preconcentration. The reproducibility of the preconcentration method (relative standard deviation (RSD)) was determined by performing five experiments from solutions containing Pb(II) and Cd(II) (50 mL, 5.0 × 10−5 g L−1). The results showed 1.27% for Pb(II) and 0.94% for Cd(II).
Table 5 shows a comparison among EgLiCl-mGO with some new adsorbents. EgLiCl-mGO has an important development in MSPE including decreasing adsorbent amount and RSD as well as widening LDR. Additionally, EgLiCl-mGO was performed in semi-neutral pH, reducing the usage of materials to pH adjustment. More importantly, EgLiCl-mGO is a green, safe, and earth-friendly adsorbent and its preparation is fast without consumption of any dangerous material. The preconcentration time is about six minutes, which is another advantage of this method.

3.8. Adsorption Isotherm

The isotherm study shows the adsorption behavior of a system such as homogenous or heterogenous distribution of the analyte onto the surface of the adsorbent. In this article, five isotherm models were applied to investigate the adsorption of Pb(II) and Cd(II) on the surface of EgLiCl-mGO. This study was conducted in the presence of EgLiCl-mGO (1.0 × 10−2 g) in the sample solution containing the analytes (50 mL) during 5 min shaking at room temperature. According to Figure S1, increasing the initial concentration of ions has a direct effect on adsorption capacity (qe) of EgLiCl-mGO, because by increasing Ce, qe increases. qe is calculated using the following equation.
q e = ( C 0 C e ) W × V
C0 is the initial concentration of the analyte, Ce is the equilibrium concentration of the analyte, V is the volume of the sample solution, and W is the amount of the adsorbent [37,38].
Langmuir is a monolayer adsorption model. It shows that the adsorbate molecules are adsorbed onto the homogeneous surface of the adsorbent. After the first layer of the analyte, no more analyte will be adsorbed onto the surface of the adsorbent. Equation (4) shows the linear form of this model.
1 q e = 1 q 0 K L C e + 1 q 0
Ce is the equilibrium concentration of heavy metals adsorbed by EgLiCl-mGO, qe is the retention capacity of analytes, KL is the Langmuir constant, showing the binding energy between the adsorbate and adsorbent; qmax is the maximum adsorption capacity of the adsorbent. The straight line was obtained when 1/qe was plotted against 1/Ce as shown in Figure S2. The slope and intercepts show the qmax and KL, respectively [38,39,40].
The Freundlich model is a multilayer adsorption model. The linear form of the Freundlich model is written in Equation (5).
ln q e = ln k f + 1 n ln C e
where Kf is the Freundlich constant, expressing the capacity, Ce defines the adsorbate concentrations of analytes, qe is the quantity of ions at equilibrium, and n is the Freundlich exponent. Kf and n were determined from plot lnqe vs. lnCe (Figure S3). The n value shows the nature of adsorption (1/n < 1: normal process), (1/n > 1: cooperative process) [38,39,40].
The Temkin isotherm depicts the interaction between the adsorbate and the adsorbent and causes a linear decrease in the adsorption energy with surface coverage of the adsorbent. Equation (6) shows the linear form of this model.
q e = R T B ln A T + R T B ln C e
where AT is the Temkin isotherm equilibrium binding constant, R of 8.314 × 103 J mol−1 K−1 is the universal gas constant, T is the absolute temperature, and B is the model constant and shows the heat of absorption [40,41]. Both B and AT can be extracted from the plot qe vs. lnCe (Figure S4).
The Halsey isotherm model expresses the multilayer adsorption of the analyte over the heterosporous adsorbent. Equation (7) shows the linear form for the model.
ln q e = ( 1 n H ) ln K H ( 1 n H ) ln C e
The Halsey isotherm model constant and Halsey isotherm model exponent are represented as KH and nH, respectively [38,40,41]. This model is plotted in Figure S5.
The Elovich model is based on multilayer adsorption, assuming exponential increasing trend in the adsorption sites as adsorption takes place. It is given by the equation below:
ln q e C e = ln ( K e q m ) q e q m
Ke and qm are the Elovich constants, representing the initial adsorption rate and maximum adsorption capacity, respectively [38,40,41]. Figure S6 shows the model.
Among the five mentioned models, Pb(II) follows the Freundlich model to be adsorbed onto EgLiCl-mGO, but Langmuir is fitted with the adsorption of Cd(II) onto EgLiCl-mGO. Therefore, the adsorption of Pb(II) onto the surface of EgLiCl-mGO is multilayered and a different layer of Pb(II) can be adsorbed onto each other but the adsorption of Cd(II) onto the surface of EgLiCl-mGO is the monolayer and after the first layer of Cd(II) no more Cd(II) is adsorbed. Isotherm parameters of each model are summarized in Table 6. R2 shows the best model for each of analyte. All the figures (Figures S1–S6) are plotted in the Electronic Supplementary Materials (ESMs).

3.9. Adsorption Kinetics

The rate and the characteristics of the adsorption of target analytes onto EgLiCl-mGO were investigated via pseudo-first-order and pseudo-second-order models. The samples of heavy metals (50 mL, 20 mg L−1) were prepared and EgLiCl-mGO (1.0 × 10−2 g L−1) was added. The adsorption of ions was followed up at different time points, ranging from 1 to 60 min at room temperature.
The pseudo-first-order kinetic modeling is provided in the following equation:
ln ( q e q t ) = ln q max k 1 t
qt (mg g−1) and k1 (min−1) are the amounts of adsorbed ions onto EgLiCl-mGO at several times and the pseudo-first-order kinetic, respectively [42,43,44,45]. Figure S7 shows the plot.
The pseudo-second-order kinetic is plotted according to Equation (10).
t q t = 1 k 2 × q c a l 2 + 1 q c a l × t
where qt (mg g−1) and k2 (g mg−1 min−1) are the amount of adsorbed analyte onto the surface of solid adsorbent at various times and the rate constant of the pseudo-second-order kinetic, respectively [42,43]. Figure S8 shows the plot.
Figures S7 and S8 are presented in the Electronic Supplementary Materials (ESMs). The R2 of the pseudo-first-order model was in the scope of 0.99 for both ions so the adsorption rate-controlling step was performed by occupying empty adsorption sites of EgLiCl-mGO by Pb(II) and Cd(II) (Table 7) [44,45,46].

3.10. Adsorption Thermodynamics

The adsorption process of heavy metals onto solid adsorbents mainly takes places via electro-static forces so it is exothermic (ΔH < 0) or endothermic (ΔH > 0) in nature. The value of ΔH is the main parameter used to distinguish chemisorption from physisorption [47]. Kd is the equilibrium constant, showing free Gibbs energy (ΔG); consequently, the enthalpy (ΔH) and the entropy ΔS of adsorption could be calculated using the following equations:
Δ G = R T ln k d
Δ G = Δ H T Δ S
where T is the absolute temperature and R is the universal gas constant (8.314 J mol−1 K−1). The plots of ln(Kd) vs. 1/T for Pb(II) and Cd(II) are shown, respectively, in Figure S9a,b in the Electronic Supplementary Materials (ESMs). The negative values of ∆G indicate the spontaneous nature of Pb(II) and Cd(II) adsorption onto EgLiCl-mGO. The positive values of ∆H demonstrate the endothermic character of the adsorption process, and ΔH more than 40 kJ mol−1 shows chemisorption and ΔH lower than 40 is related to chemisorption. The positive values of ∆S indicate the increase in disorder at the solid–liquid interface as well as more agitation in the sample solution due to releasing water molecules that grab the ions [48,49,50]. The obtained results are shown in Table 8.

4. Discussion

In the present study, a novel nanocomposite (EgLiCl-mGO) was successfully synthesized and applied as an efficient adsorbent in the MSPE procedure of Pb(II) and Cd(II) ions. The nanocomposite combining DES had the advantage of superparamagnetism, low environmental pollution, good water dispersibility, rapid extraction, and reproducibility; in the meantime, it showed excellent selectivity for Pb(II) and Cd(II). Moreover, its structural and magnetic properties were confirmed by FT-IR, VSM, and XRD. For the MSPE procedure, the affecting parameters on adsorption and desorption steps were optimized via the one-at-a-time method. LOD, LOQ, PF, EF, RSD, selectivity, effect of interference ions, selectivity, swelling behavior, isotherm adsorption, kinetic adsorption, and thermodynamic adsorption were investigated in detail. The technique was applied successfully to preconcentrate Pb(II) and Cd(II) simultaneously in four legume samples.

5. Conclusions

This article confirmed that EgLiCl-mGO is a qualified adsorbent to simultaneously preconcentrate ultratrace amounts of Pb(II) and Cd(II) in legumes. In additional to acceptable analytical results, this adsorbent is easy to prepare without consumption of dangerous and harmful reagents. The EgLiCl-mGO is an energy efficient and environmentally friendly adsorbent.

Supplementary Materials

The following supporting information can be downloaded at: https://www.mdpi.com/article/10.3390/app13095702/s1, This article includes Electronic Supplementary Materials (ESMs). FT-IR analysis, Effect of initial concentrations of a Pb(II) and b Cd(II) on adsorption capacity of EgLiCl-mGO, Langmuir model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, Freundlich model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, Temkin model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, Halsey model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, Elovich model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, the first-order kinetic model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO, the first-order kinetic model of a Pb(II) and b Cd(II) adsorptions onto EgLiCl-mGO and thermodynamic parameters, enthalpy and entropy for the adsorption of a Pb(II) and b Cd(II) onto EgLiCl-mGO are provided in ESMs.

Author Contributions

Conceptualization: P.J. and M.H.; Methodology: P.J. and M.H.; Validation; P.J.; Formal Analysis: P.J. and M.H.; Investigation: P.J.; Resource; P.J. and M.H.; Data Curation: P.J.; Writing—Original Draft Preparation: P.J. and M.H.; Writing—Review and Editing: P.J. and M.H.; Supervision: P.J.; Project Administartion: P.J. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Institutional Review Board Statement

Not applicable.

Informed Consent Statement

Not applicable.

Data Availability Statement

The data presented in this study are available on request from the corresponding author.

Acknowledgments

Support for this study by the Research Council of the University of Tehran through grants is gratefully acknowledged.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Perna, F.M.; Vitale, P.; Capriati, V. Deep eutectic solvents and their applications as green solvents. Curr. Opin. Green Sustain. Chem. 2020, 21, 27–33. [Google Scholar] [CrossRef]
  2. Socas-Rodríguez, B.; Torres-Cornejo, M.V.; Álvarez-Rivera, G.; Mendiola, J.A. Deep Eutectic Solvents for the Extraction of Bioactive Compounds from Natural Sources and Agricultural By-Products. Appl. Sci. 2021, 11, 4897. [Google Scholar] [CrossRef]
  3. Hansen, B.B.; Spittle, S.; Chen, B.; Poe, D.; Zhang, Y.; Klein, J.M.; Horton, A.; Adhikari, L.; Zelovich, T.; Doherty, B.W.; et al. Deep Eutectic Solvents: A Review of Fundamentals and Applications. Chem. Rev. 2021, 121, 1232–1285. [Google Scholar] [CrossRef]
  4. Moura, L.; Moufawad, T.; Ferreira, M.; Bricout, H.; Tilloy, S.; Monflier, E.; Costa Gomes, M.F.; Landy, D.; Fourmentin, S. Deep eutectic solvents as green absorbents of volatile organic pollutants. Environ. Chem. Lett. 2017, 15, 747–753. [Google Scholar] [CrossRef]
  5. Rodríguez-Ramos, R.; Santana-Mayor, Á.; Socas-Rodríguez, B.; Rodríguez-Delgado, M.Á. Recent Applications of Deep Eutectic Solvents in Environmental Analysis. Appl. Sci. 2021, 11, 4779. [Google Scholar] [CrossRef]
  6. Alomar, T.S.; Habila, M.A.; AlMasou, N.; Alothman, Z.A.; Sheikh, M.; Soylak, M. Biomass-Derived Adsorbent for Dispersive Solid-Phase Extraction of Cr(III), Fe(III), Co(II) and Ni(II) from Food Samples Prior to ICP-MS Detection. Appl. Sci. 2021, 11, 7792. [Google Scholar] [CrossRef]
  7. Plastiras, O.E.; Deliyanni, E.; Samanidou, V. Synthesis and Application of the Magnetic Nanocomposite GO-Chm for the Extraction of Benzodiazepines from Surface Water Samples Prior to HPLC-PDA Analysis. Appl. Sci. 2021, 11, 7828. [Google Scholar] [CrossRef]
  8. Hejazi Khah, M.; Jamshidi, P.; Shemirani, F. Applying Fe3O4-MoS2-chitosan nanocomposite to preconcentrate heavy metals from dairy products prior quantifying by FAAS. Res. Chem. Intermed. 2021, 47, 3867–3881. [Google Scholar] [CrossRef]
  9. Bhaskar, S.; Visweswar Kambhampati, N.S.; Ganesh, K.M.; Sharma, P.M.; Srinivasan, V.; Ramamurthy, S.S. Metal-Free, Graphene Oxide-Based Tunable Soliton and Plasmon Engineering for Biosensing Applications. ACS Appl. Mater. Interfaces 2021, 13, 17046–17061. [Google Scholar] [CrossRef]
  10. Rai, A.; Bhaskar, S.; Ganesh, K.M.; Ramamurthy, S.S. Engineering of coherent plasmon resonances from silver soret colloids, graphene oxide and Nd2O3 nanohybrid architectures studied in mobile phone-based surface plasmon-coupled emission platform. Mater. Lett. 2021, 304, 130632. [Google Scholar] [CrossRef]
  11. Khalilifard, M.; Javadian, S. Magnetic superhydrophobic polyurethane sponge loaded with Fe3O4@oleic acid@graphene oxide as high performance adsorbent oil from water. Chem. Eng. J. 2021, 408, 127369. [Google Scholar] [CrossRef]
  12. Khawaja, H.; Zahir, E.; Asghar, M.A.; Asghar, M.A. Graphene oxide decorated with cellulose and copper nanoparticle as an efficient adsorbent for the removal of malachite green. Int. J. Biolog. Macromol. 2021, 167, 23–34. [Google Scholar] [CrossRef] [PubMed]
  13. Ibrahim, R.K.; El-Shafie, A.; Hin, L.S.; Mohd, N.S.B.; Aljumaily, M.M.; Ibraim, S.; AlSaadi, M.A. A clean approach for functionalized carbon nanotubes by deep eutectic solvents and their performance in the adsorption of methyl orange from aqueous solution. J. Environ. Manag. 2019, 235, 521–534. [Google Scholar] [CrossRef] [PubMed]
  14. Wang, X.; Li, G.; Row, K.H. Graphene and Graphene Oxide Modified by Deep Eutectic Solvents and Ionic Liquids Supported on Silica as Adsorbents for Solid-Phase Extraction. Bull. Korean Chem. Soc. 2017, 38, 251–257. [Google Scholar] [CrossRef]
  15. Lomba, L.; García, C.B.; Ribate, M.P.; Giner, B.; Zuriaga, E. Applications of Deep Eutectic Solvents Related to Health, Synthesis, and Extraction of Natural Based Chemicals. Appl. Sci. 2021, 11, 10156. [Google Scholar] [CrossRef]
  16. Kamel, A.H.; Amr, A.E.G.E.; Al-Omar, M.A.; Elsayed, A.E. Pre-Concentration Based on Cloud Point Extraction for Ultra-Trace Monitoring of Lead (II) Using Flame Atomic Absorption Spectrometry. Appl. Sci. 2019, 9, 4752. [Google Scholar] [CrossRef]
  17. Alotaibi, K.M.; Almethen, A.A.; Beagan, A.M.; Al-Swaidan, H.M.; Ahmad, A.; Bhawani, S.A.; Alswieleh, A.M. Quaternization of Poly(2-diethyl aminoethyl methacrylate) Brush-Grafted Magnetic Mesoporous Nanoparticles Using 2-Iodoethanol for Removing Anionic Dyes. Appl. Sci. 2021, 11, 10451. [Google Scholar] [CrossRef]
  18. Wang, S.; Li, X.; Li, M.; Li, X.; Li, X.; Li, S.; Zhang, Q.; Li, H. Self-Assembled Three-Dimensional Microporous rGO/PNT/Fe3O4 Hydrogel Sorbent for Magnetic Preconce.ntration of Multi-Residue Insecticides. Appl. Sci. 2020, 10, 5665. [Google Scholar] [CrossRef]
  19. Huang, X.; Liu, G.; Xu, D.; Xu, X.; Li, L.; Zheng, S.; Lin, H.; Gao, H. Novel Zeolitic Imidazolate Frameworks Based on Magnetic Multiwalled Carbon Nanotubes for Magnetic Solid-Phase Extraction of Organochlorine Pesticides from Agricultural Irrigation Water Samples. Appl. Sci. 2018, 8, 959. [Google Scholar] [CrossRef]
  20. Jamshidi, P.; Shemirani, F. Adsorption/desorption of acid violet-7 onto magnetic MnO2 prior to its quantification by UV–visible spectroscopy: Optimized by fractional factorial design. Res. Chem. Intermed. 2020, 46, 4403–4422. [Google Scholar] [CrossRef]
  21. Nishina, Y.; Eigler, S. Chemical and electrochemical synthesis of graphene oxide–a generalized view. Nanoscale 2020, 12, 12731–12740. [Google Scholar] [CrossRef] [PubMed]
  22. Sujiono, E.H.; Zabrian, D.; Dahlan, M.; Amin, B.; Agus, J. Graphene oxide based coconut shell waste: Synthesis by modified Hummers method and characterization. Heliyon 2020, 6, e04568. [Google Scholar] [CrossRef] [PubMed]
  23. Dana, M.; Jamshidi, P.; Shemirani, F. Acid Brown-14 preconcentration onto an adsorbent consisting of Fe3O4, carbon nanotube and CeO: Optimized by a multi-variable method. Res. Chem. Intermed. 2021, 47, 1021–1032. [Google Scholar] [CrossRef]
  24. Hejazi Khah, M.; Jamshidi, P.; Shemirani, F. Applicability of an eco-friendly deep eutectic solvent loaded onto magnetic graphene oxide to preconcentrate trace amount of indigotin blue dye. J. Mol. Liq. 2021, 342, 117346. [Google Scholar] [CrossRef]
  25. Workie, Y.A.; Sabrina Imae, T.; Krafft, M.P. Nitric oxide gas delivery by fluorinated poly (Ethylene Glycol)@ graphene oxide carrier toward pharmacotherapeutics. ACS Biomater. Sci. Eng. 2019, 5, 2926–2934. [Google Scholar] [CrossRef]
  26. Majid, F.; Ali, M.D.; Ata, S.; Bibi, I.; Malik, A.; Ali, A.; Alwadai, N.; Albalawi, H.; Shoaib, M.; Bukhari, S.A.; et al. Fe3O4/graphene oxide/Fe4[Fe(CN)6]3 nanocomposite for high performance electromagnetic interference shielding. Ceram. Int. 2021, 47, 11587–11595. [Google Scholar] [CrossRef]
  27. Ma, Z.; Guan, Y.; Liu, H. Synthesis and characterization of micron-sized monodisperse superparamagnetic polymer particles with amino groups. J. Polym. Sci. A Polym. Chem. 2005, 43, 3433–3439. [Google Scholar] [CrossRef]
  28. Faryadras, F.; Yousefi, S.M.; Jamshidi, P.; Shemirani, F. Application of magnetic graphene-based bucky gel as an efficient green sorbent for determination of mercury in fish and water samples. Res. Chem. Intermed. 2020, 46, 2055–2068. [Google Scholar] [CrossRef]
  29. Zhang, J.; Wang, L.; Wang, A. Preparation and Properties of Chitosan-g-poly(acrylic acid)/Montmorillonite Superabsorbent Nanocomposite via in Situ Intercalative Polymerization. Ind. Eng. Chem. Res. 2007, 46, 2497–2502. [Google Scholar] [CrossRef]
  30. Shuyue, J.; Dongyan, T.; Jing, P.; Xu, Y.; Zhaojie, S. Crosslinked electrospinning fibers with tunable swelling behaviors: A novel and effective adsorbent for Methylene Blue. Chem. Eng. J. 2020, 390, 124472. [Google Scholar] [CrossRef]
  31. Jamshidi, P.; Alvand, M.; Shemirani, F. Magnetic Mn2O3 nanocomposite covered with N,N′-bis(salicylidene)ethylenediamine for selective preconcentration of cadmium(II) prior to its quantification by FAAS. Microchim. Acta 2019, 186, 487. [Google Scholar] [CrossRef] [PubMed]
  32. Fei, J.J.; Zhao, L.Y.; Wu, X.H.; Cui, X.B.; Min, H.; Lian, H.Z.; Chen, Y.J. In-tube solid-phase microextraction with a hybrid monolithic column for the preconcentration of ultra-trace metals prior to simultaneous determination by ICP-MS. Microchim. Acta 2020, 187, 356. [Google Scholar] [CrossRef] [PubMed]
  33. Kobylinska, N.; Kostenko, L.; Khainakov, S.; Garcia-Granda, S. Advanced core-shell EDTA-functionalized magnetite nanoparticles for rapid and efficient magnetic solid phase extraction of heavy metals from water samples prior to the multi-element determination by ICP-OES. Microchim. Acta 2020, 187, 289. [Google Scholar] [CrossRef] [PubMed]
  34. Sorouraddin, S.M.; Farajzadeh, M.A.; Dastoori, H. Development of a dispersive liquid-liquid microextraction method based on a ternary deep eutectic solvent as chelating agent and extraction solvent for preconcentration of heavy metals from milk samples. Talanta 2020, 208, 120485. [Google Scholar] [CrossRef] [PubMed]
  35. Shirani, M.; Salari, F.; Habibollahi, S.; Akbari, A. Needle hub in-syringe solid phase extraction based a novel functionalized biopolyamide for simultaneous green separation/preconcentration and determination of cobalt, nickel, and chromium (III) in food and environmental samples with micro sampling flame atomic absorption spectrometry. Microchem. J. 2020, 152, 104340. [Google Scholar]
  36. Ozdemir, S.; Kılınç, E.; Acer, Ö.; Soylak, M. Simultaneous preconcentrations of Cu(II), Ni(II), and Pb(II) by SPE using E. profundum loaded onto Amberlite XAD-4. Microchem. J. 2021, 171, 106758. [Google Scholar] [CrossRef]
  37. Jamshidi, P.; Shemirani, F. Adsorption and desorption of Pb2+ on magnetic Mn2O3 as highly efficient adsorbent: Isotherm, kinetic and thermodynamic studies. Colloids Surf. A Physicochem. Eng. Asp. 2019, 571, 151–159. [Google Scholar] [CrossRef]
  38. Brdar, M.; Šćiban, M.; Takači, A.; Došenović, T. Comparison of two and three parameters adsorption isotherm for Cr(VI) onto Kraft lignin. Chem. Eng. J. 2012, 183, 108–111. [Google Scholar] [CrossRef]
  39. Nait-Merzoug, A.; Guellati, O.; Djaber, S.; Habib, N.; Harat, A.; El-Haskouri, J.; Begin, D.; Guerioune, M. Ni/Zn Layered Double Hydroxide (LDH) Micro/Nanosystems and Their Azorubine Adsorption Performance. Appl. Sci. 2021, 11, 8899. [Google Scholar] [CrossRef]
  40. Rajahmundry, G.K.; Garlapati, C.; Kumar, P.S.; Alwi, R.S.; Vo, D.V.N. Statistical analysis of adsorption isotherm models and its appropriate selection. Chemosphere 2021, 276, 130176. [Google Scholar] [CrossRef]
  41. Jamshidi, P.; Shemirani, F. Synthesis of a magnetic WO3 nanocomposite for use in highly selective preconcentration of Pb(II) prior to its quantification by FAAS. Microchim. Acta 2018, 185, 421. [Google Scholar] [CrossRef] [PubMed]
  42. Tejada-Tovar, C.; Villabona-Ortíz, Á.; Gonzalez-Delgado, D. Removal of Nitrate Ions Using Thermally and Chemically Modified Bioadsorbents. Appl. Sci. 2021, 11, 8455. [Google Scholar] [CrossRef]
  43. Ukkund, S.J.; Puthiyillam, P.; Alshehri, H.M.; Goodarzi, M.; Taqui, S.N.; Anqi, A.E.; Safaei, M.R.; Ali, M.A.; Syed, U.T.; Mir, R.A.; et al. Adsorption Method for the Remediation of Brilliant Green Dye Using Halloysite Nanotube: Isotherm, Kinetic and Modeling Studies. Appl. Sci. 2021, 11, 8088. [Google Scholar] [CrossRef]
  44. Singh, S.; Kapoor, D.; Khasnabis, S.; Singh, J.; Ramamurthy, P.C. Mechanism and kinetics of adsorption and removal of heavy metals from wastewater using nanomaterials. Environ. Chem. Lett. 2021, 19, 2351–2381. [Google Scholar] [CrossRef]
  45. Ighalo, J.O.; Adeniyi, A.G.; Eletta, O.A.A.; Arowoyele, L.T. Competitive adsorption of Pb(II), Cu(II), Fe(II) and Zn(II) from aqueous media using biochar from oil palm (Elaeis guineensis) fibers: A kinetic and equilibrium study. Indian Chem. Eng. 2021, 63, 501–511. [Google Scholar] [CrossRef]
  46. Zhang, X.; Yan, L.; Li, J.; Yu, H. Adsorption of heavy metals by l-cysteine intercalated layered double hydroxide: Kinetic, isothermal and mechanistic studies. J. Colloid Interface Sci. 2020, 562, 149–158. [Google Scholar] [CrossRef]
  47. Abbou, B.; Lebkiri, I.; Ouaddari, H.; Kadiri, L.; Ouass, A.; Habssaoui, A.; Lebkiri, A.; El Housseine, R. Removal of Cd (II), Cu (II), and Pb (II) by adsorption onto natural clay: A kinetic and thermodynamic study. Turk. J. Chem. 2021, 45, 362–376. [Google Scholar] [CrossRef]
  48. Nistor, M.A.; Muntean, S.G.; Ianoș, R.; Racoviceanu, R.; Ianași, C.; Cseh, L. Adsorption of Anionic Dyes from Wastewater onto Magnetic Nanocomposite Powders Synthesized by Combustion Method. Appl. Sci. 2021, 11, 9236. [Google Scholar] [CrossRef]
  49. Abbas, M.; Trari, M. Kinetic, equilibrium and thermodynamic study on the removal of Congo Red from aqueous solutions by adsorption onto apricot stone. Process. Saf. Environ. Prot. 2015, 98, 424–436. [Google Scholar] [CrossRef]
  50. Nadarajah, K.; Bandala, E.R.; Zhang, Z.; Mundree, S.; Goonetilleke, A. Removal of heavy metals from water using engineered hydrochar: Kinetics and mechanistic approach. J. Water Process. Eng. 2021, 40, 101929. [Google Scholar] [CrossRef]
Figure 1. FT-IR spectra of mGO and EgLiCl-mGO.
Figure 1. FT-IR spectra of mGO and EgLiCl-mGO.
Applsci 13 05702 g001
Figure 2. (a) The XRD pattern of EgLiCl-mGO; (b) magnetic hysteresis loops image of EgLiCl-mGO.
Figure 2. (a) The XRD pattern of EgLiCl-mGO; (b) magnetic hysteresis loops image of EgLiCl-mGO.
Applsci 13 05702 g002
Table 1. Results of different eluents (1 mL) on the preconcentration of Pb(II) and Cd(II) (n = 3).
Table 1. Results of different eluents (1 mL) on the preconcentration of Pb(II) and Cd(II) (n = 3).
Recovery
(%)
Eluent
Cd(II)Pb(II)
60.52 ± 0.0341.23 ± 0.01HNO3 (1 mol L−1)
98.14 ± 0.0599.34 ± 0.07HNO3 (2 mol L−1)
84.48 ± 0.1176.15 ± 0.13HNO3 (5 mol L−1)
14.96 ± 0.1024.94 ± 0.14HCl (1 mol L−1)
22.46 ± 0.1511.16 ± 0.11HCl (2 mol L−1)
5.63 ± 0.084.63 ± 0.11HCl (5 mol L−1)
Table 2. Swelling behavior of EgLiCl-mGO to adsorb Pb(II) and Cd(II) at different pH.
Table 2. Swelling behavior of EgLiCl-mGO to adsorb Pb(II) and Cd(II) at different pH.
pHWd
(×10−2 g)
Ws
(×10−2 g)
SD
21.01.70.7
31.06.35.3
41.09.38.3
51.08.27.2
61.07.96.9
71.06.05.0
81.03.12.1
91.02.11.1
Table 3. The interfering effect of various ions on preconcentrating Pb(II) and Cd(II) (n = 3).
Table 3. The interfering effect of various ions on preconcentrating Pb(II) and Cd(II) (n = 3).
IonsRatio of Coexisting IonsRecovery
(%)
Pb(II)Cd(II)
Na(I)10,00096.03 ± 0.1298.14 ± 0.09
K(I)10,00098.12 ± 0.2797.43 ± 0.11
Li(I)80099.17 ± 0.1499.14 ± 0.08
Ca(II)500100.56 ± 0.2199.17 ± 0.05
Mg(II)30098.08 ± 0.1896.13 ± 0.04
Cr(II)20097.03 ± 0.2499.94 ± 0.18
Pd(II)80097.26 ± 0.1998.32 ± 0.11
Zn(II)250102.45 ± 0.11100.32 ± 0.10
Al(III)70099.69 ± 0.2798.71 ± 0.07
Mn(II)50097.34 ± 0.1896.52 ± 0.04
Co(II)10098.98 ± 0.35101.43 ± 0.01
Cu(II)10096.15 ± 0.2896.83 ± 0.04
Ni(II)10095.28 ± 0.1799.54 ± 0.9
SO42−100095.35 ± 0.3198.18 ± 0.13
Cl100097.53 ± 0.24100.32 ± 0.15
NO3100099.18 ± 0.1999.54 ± 0.09
CO32−1000101.37 ± 0.20100.91 ± 0.11
Table 4. Analytical results of Pb(II) and Cd(II) quantified by EgLiCl-mGO (n = 3).
Table 4. Analytical results of Pb(II) and Cd(II) quantified by EgLiCl-mGO (n = 3).
SampleSpiked
(g L−1)
FoundRecovery
(%)
FoundRecovery
(%)
Cd(II)Pb(II)
Kidney bean01.84-2.46-
5.0 × 10−552.91102.1454.26103.43
Cowpea01.34-1.76-
5.0 × 10−549.6596.9749.6497.79
Pinto bean03.11-2.95-
5.0 × 10−551.9897.8750.7595.84
Navy bean00.95-4.76-
5.0 × 10−552.04102.1554.3899.30
Table 5. Comparison of the proposed technique with several recent methods for simultaneous determination of heavy metals (FAAS was used for all detections).
Table 5. Comparison of the proposed technique with several recent methods for simultaneous determination of heavy metals (FAAS was used for all detections).
MethodAmount
(g)
LOD
(g L−1)
RSD
(%)
PFLDR
(g L−1)
Reference
SPE-6 × 10−6–12 × 10−61.0–2.21000.5 × 10−6–100 × 10−6[32]
MSPE5.0 × 10−20.06 × 10−6–0.76 × 10−6 0.18–3.101500.1 × 10−6–200 × 10−6[33]
LLE-0.38 × 10−6–0.42 × 10−63.6–5.2-1.0 × 10−6–40 × 10−6[34]
SPE4.0 × 10−32.74 × 10−6–3.10 × 10−63.2–3.550-[35]
SPE-0.031 × 10−6–0.043 × 10−62.44–4.68 0.25 × 10−6–25 × 10−6[36]
MSPE1.0 × 10−247 × 10−8–1.2 × 10−60.94–1.27505.0 × 10−6–4.0 × 10−4 g L−1This work
Table 6. Adsorption isotherms for Pb(II) and Cd(II) onto EgLiCl-mGO.
Table 6. Adsorption isotherms for Pb(II) and Cd(II) onto EgLiCl-mGO.
ModelPb(II)Cd(II)
ParametersR2ParametersR2
Langmuirq0 = 75.18
KL = 2.83
0.99q0 = 50
KL = 1.45
0.90
Freundlichn = 4.52
Kf = 45.36
0.89n = 2.48
Kf = 24.77
0.99
TemkinB = 233.31
AT = 100.48
0.92B = 178.38
AT = 7.02
0.93
Elovichqm = 1.51
KE = 727.18
0.86qm = 25.1
KE = 2.76
0.90
Halseyn = −4.52
KH = 31.6 × 106
0.86n = −2.4
KH = 2.9 × 103
0.97
Table 7. Comparison of kinetic models for Pb(II) and Cd(II) adsorption onto EgLiCl-mGO.
Table 7. Comparison of kinetic models for Pb(II) and Cd(II) adsorption onto EgLiCl-mGO.
AnalyteModelParametersValuesR2
Pb(II)Pseudo first orderk1 (min−1)
qe (mg g−1)
0.03
95.40
0.99
Pseudo second orderk2 (g mg−1 min−1)
qe (mg g−1)
4.04 × 10−4
111.11
0.95
Cd(II)Pseudo first orderk1 (min−1)
qe (mg g−1)
0.023
67.46
0.99
Pseudo second orderk2 (g mg−1 min−1)
qe (mg g−1)
1.7 × 10−3
88.49
0.98
Table 8. Thermodynamic parameters for the Pb(II) and Cd(II) adsorption onto EgLiCl-mGO.
Table 8. Thermodynamic parameters for the Pb(II) and Cd(II) adsorption onto EgLiCl-mGO.
TPb(II)Cd(II)
Ce
(mg L−1)
qe
(mg g−1)
ΔG
(J mol−1)
Ce
(mg L−1)
qe
(mg g−1)
ΔG
(J mol−1)
27328.656.75358125.4322.85265
28326.4317.8597223.4532.75−827
29822.9135.45−108120.8545.75−1946
31814.6576.75−410317.7661.2−3065
3437.13114.35−687512.2188.95−4920
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Hejazikhah, M.; Jamshidi, P. Modification of Magnetic Graphene Oxide by an Earth-Friendly Deep Eutectic Solvent to Preconcentrate Ultratrac Amounts of Pb(II) and Cd(II) in Legume Samples. Appl. Sci. 2023, 13, 5702. https://doi.org/10.3390/app13095702

AMA Style

Hejazikhah M, Jamshidi P. Modification of Magnetic Graphene Oxide by an Earth-Friendly Deep Eutectic Solvent to Preconcentrate Ultratrac Amounts of Pb(II) and Cd(II) in Legume Samples. Applied Sciences. 2023; 13(9):5702. https://doi.org/10.3390/app13095702

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Hejazikhah, Melika, and Parastoo Jamshidi. 2023. "Modification of Magnetic Graphene Oxide by an Earth-Friendly Deep Eutectic Solvent to Preconcentrate Ultratrac Amounts of Pb(II) and Cd(II) in Legume Samples" Applied Sciences 13, no. 9: 5702. https://doi.org/10.3390/app13095702

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