Abstract

A kind of Sr2+ selective resin was applied as an absorption phase to extract Sr2+ ion from an aqueous solution, and the amount of Sr2+ was determined using inductively coupled plasma optical emission spectrometer. Factors, including absorption time, temperature, stirring rate, salt-out effect, desorption, and the pH of the aqueous solution, were investigated to optimize the absorption efficiency of Sr2+. Foreign ions were examined to observe their effects on the absorption behavior of Sr2+. The optimum condition was absorption time at 20 min, pH of aqueous solution 7, temperature of 35°C, and 600 rpm stirring rate. A 10 mL solution of 0.1 mol/L HCl is used as the desorption agent. The linear range of Sr2+ concentrations from 50 to 1200 μg/L was investigated with the slope of 183 μg/L. The limit of detection was 21 μg/L with 4.23% relative standard deviation. The correlation coefficient was found to be 0.9947. Under the optimized conditions, the concentrations of Sr2+ in four water samples were detected by the developed method. We propose that this method effectively extracts strontium ion from environmental water samples.

1. Introduction

Strontium and its isotopes as effective tracers are applied for characterizing geochemical and biogeochemical behaviors in the fields of archaeology [1, 2], water-rock interactions [3], and geologic chronology [4] to identify and trace the origins and evolutions of the climate and the environment [5, 6]. The separation of strontium from alkali and alkaline-earth elements is important for the determination of strontium isotopic composition in natural sample and for the isotopic detection of 87Sr and 87Rb by thermal ionization mass spectrometry (TIMS) or multicollector inductively coupled plasma mass spectrometry.

Commonly, natural strontium compounds coexist with other alkali and alkaline-earth compounds, such as sodium, calcium, magnesium, and barium compounds, which make the separation of strontium more complex. Fuming nitric acid has been used previously to separate strontium from large quantities of alkali, alkaline-earth, and other elements effectively [710].

Recently, the methods for strontium ion separation have been developed to avoid employing toxic fuming nitric acid to separate strontium, a method previously developed by Grahek et al. [11]. The methods include the use of ion-exchange resins [12, 13], dispersive liquid phase microextraction [14, 15], and strontium specific resins [16]. By these methods, strontium ion was separated along with other alkaline-earth elements that demonstrate similar chemical behaviors [7]. Furthermore, alkali elements, such as sodium, potassium, rubidium, and others, interfered with the strontium separation.

In recent years, ion imprinting has been considered as a convenient and powerful method for synthesizing polymers in the presence of desired template ions [17, 18]. Silica gel is used as a support for ion imprinting due to its chemical, mechanical, and thermal stability and low cost [710]. The objective of this study is to utilize a Sr2+ selective polymer in the presence of silica gel to separate Sr2+ in water sample. In the following experiments, the Sr2+ selective polymer is used as an absorbent phase for the extraction of Sr2+, and the absorbent behaviors of the Sr2+ selective polymer are investigated. The factors influencing the efficiency of Sr2+ ion extraction, such as absorption time, pH in the aqueous solution, temperature, stirring rate, salt-out effect, and desorption solution, were optimized. In the optimum conditions, the characteristics of the described method were evaluated, and four real water samples were utilized to assess the applicability and reliability of the proposed method.

2. Material and Methods

2.1. Instruments

An inductively coupled plasma optical emission spectrometer (ICP-OES, Vista MPX, Varian, USA) with a 40 MHz radio frequency generator and a charge-coupled device detector (Vista Chip) was used to detect strontium ion. The spectrometer was operated in a transient signal acquisition mode [15]. An axial-viewing quartz torch, a cyclonic spray chamber, a glass concentric nebulizer, and a peristaltic pump were used. The measurements were carried out at a radio frequency generator power of 1.0 kW, plasma gas flow rate of  15.0 L/min, auxiliary gas flow rate of 1.5 L/min, nebulizer gas pressure of 200 kPa, replicate read time of 5 s, and pump rate of 15 rpm.

2.2. Reagents and Materials

Strontium chloride, nitric acid, sodium hydroxide, hydrochloric acid, and sodium hydroxide were analytical grade reagents. A strontium standard solution of 100 μg/mL was purchased from the National Research Center for Certified Reference Materials (Beijing, China). Stock and working standards were prepared with deionized water.

2.3. Sr2+ Absorption Experiments

To prepare a sample, 5 g of wet gel particles was dispersed in 10 mL SrCl2 solution (5 mmol/L). HCl and NaOH solutions were used to adjust pH of the solution, and NaCl solution was used to examine the salt-out effect on the absorption efficiency of Sr2+ in the aqueous solution. The concentration of Sr2+ in the aqueous phase was determined by ICP-OES.

2.4. Selective Recognition Experiments

The absorption experiments were performed in a magnetically heated water bath at a desired temperature. The amount of Sr2+ absorbed by the particle (, in mg per g of dried particle) was calculated by a mass balance relationship, expressed as inHere, and are the Sr2+ concentrations in the solution before and after absorption, respectively. is the volume of the solution (mL), and is the amount of the absorbent (g). Ions K+, Ca2+, Ba2+, Rb+, Cs+, and Mg2+ were utilized as competitive ions at a concentration of 5.0 mg/mL to determine the selective recognition of Sr2+.

3. Results and Discussion

In this study, a Sr2+ selective polymer was used as absorbent substrate to extract Sr2+ from the aqueous phase. To optimize the absorption conditions for Sr2+ recovery, the effects of pH, absorption time, stirring rate, temperature, and salt concentration were studied. A series of designed experiments was performed.

3.1. Effect of Absorption Time on the Efficiency of Sr2+

The absorption time critically affects the efficiency of Sr2+ absorption in the aqueous phase by the polymer. In this work, a time range of 10 to 120 min was investigated while holding other parameters constant. It can be seen from Figure 1 that with the change of time to 20 min, the absorbed amount of Sr2+ levels off, implying that the absorption equilibrium was reached. The time for absorption equilibrium was fixed at 20 min for all experiments.

3.2. Effect of pH on Absorption Quantity of Sr2+

Solution pH has been found to influence complex formation of metal ions and the hydrolysis of cations [19], so pH was varied from 1 to 7 to test the absorption efficiency of Sr2+. When the pH ranges from 8 to 14, some ions would precipitate out of solution; thus, basic solutions were not considered for tests. The pH was adjusted with a solution of HCl solution. In Figure 2, it shows that the maximum efficiency for Sr2+ absorption is achieved at pH 6 and 7. At low pH, efficiency is poor because of hydrogen bonding with the polymer, which reduces the bonding availability for strontium ions. For subsequent experiments, a pH of 7 was employed.

3.3. Effect of Temperature on Absorption Quantity of Sr2+

During extraction, temperature has an important impact on the absorption efficiency of the target in aqueous solution. At high temperature, the diffusion coefficient of strontium ion in aqueous solution is higher, and the absorption time may be shortened [20]. The effect of temperature was studied by evaluating absorption temperature at 28, 35, 40, 45, 50, and 60°C. Figure 3 shows minimal differences in absorption at the temperatures studied. Although the absorption rate is accelerated with increasing temperature, the partition coefficient depends on temperature, so the effect of temperature on absorption efficiency is not significant. Thus, 35°C was chosen for the subsequent experiments.

3.4. Effect of Stirring Rate on Absorption Quantity of Sr2+

During absorption, polymer precipitates out of solution, reducing the absorption efficiency and the interaction between the polymer and the aqueous solution. Magnetic stirring was considered for the method tests. A stirring rate, ranging from 0 to 800 rpm, was taken into consideration. Figure 4 suggests that the quantity of absorbed Sr2+ saturated at stirring rate of more than 600 rpm. A stirring rate of 600 rpm was chosen for the next works.

3.5. Salt-Out Effect on Absorption Quantity of Sr2+

Salt-out effects can also influence solubility in aqueous solutions, and NaCl solution was used to adjust the ionic strength of the aqueous solution. NaCl was added in concentrations ranging from 0 to 0.2 g/mL. It can be seen from Figure 5 that the Sr2+ absorption efficiency is not sensitive to salt-out effects at NaCl concentrations in this range. As NaCl concentration increases, the ion strength of the aqueous solution increases, while the presence of Na+ ion reduces the ability of the polymer to form a complex with Sr2+ ion. Thus, NaCl was not used to adjust the ionic strength of subsequent solutions.

3.6. Desorption of Sr2+

After completing the absorption of Sr2+ ion, desorption of Sr2+ was studied using HCl solution as desorption agent. HCl solutions (10 mL) of various concentrations from 0.01 to 0.5 mol/L were used to rinse the polymer resin to investigate the absorption amount of Sr2+ at room temperature, as shown in Figure 6. Ten milliliter of 0.1 mol/L HCl solution was sufficient to rinse Sr2+ ion out of the particles completely.

3.7. Ion Interference

Foreign ions, such as K+, Ca2+, Ba2+, Rb+, Cs+, and Mg2+ ions, can interfere with the absorption of Sr2+ in aqueous solution when using the described method. To investigate the effects of foreign ions, a 10 mL solution of 100 μg/L Sr2+ mixed with these interfering ions was treated according to the procedure mentioned above. Tolerance limits for interfering ions were established as the highest concentrations that allowed strontium recovery to remain in excess of 90%. The results show that Ca2+, Mg2+, and Ba2+ could be tolerated up to concentrations of 85 μg/L, while K+ and Rb+ could be tolerated up to a concentration of 100 μg/L. The 85 μg/L of Cs+ had no significant effect on the extraction of Sr2+.

3.8. Analytical Performance

Under optimal conditions, characteristics for the extraction of Sr2+ by the method discussed above were obtained. The linear range of absorbed amount of Sr(II) by the polymer was between 50 and 1200 μg/L, and the limit of detection of this method is 21 μg/L with 4.23% of relative standard deviation. The method characteristics are shown in Table 1.

3.9. Analysis of Water Samples

Four environmental water samples were used to assess the applicability and reliability of the proposed method. The underground water sample was taken from a local well, tap water was collected from our lab, and river water samples were collected from the Yi River, in Linyi, China, at two locations. Sr2+ ions in these samples were extracted and analyzed by the above method and ICP-OES. 50 mL of each water sample was spiked with a 100 μg/L of Sr2+ standard solution. The results are listed in Table 2, which indicate that in all cases the recovery of Sr2+ from water can be quantitative.

4. Conclusions

In this study, a strontium selective polymer was used to extract Sr2+ in water sample, and the efficiency was quantified with ICP-OES. The experiment conditions and foreign ions influencing the absorption efficiency of Sr2+ on the polymer were investigated. The linear range and limit of detection of the present method are sufficient for the detection of strontium ion. Four real water samples were utilized to evaluate the applicability and reliability of the proposed method. The results suggest that the method will be useful for the extraction and quantification of strontium ion in the environmental samples.

Conflict of Interests

The author declares that there is no conflict of interests regarding the publication of this paper.

Acknowledgments

This work was supported by the Program for Natural Science Foundation of China (Grants nos. 41403005 and 41201228), the Program for Natural Science Foundation of Shandong Province, China (Grant no. ZR2014DL007), and the Project of Shandong Province Higher Educational Science and Technology Program (Grant no. J15LC11).