INTRODUCTION
Cadmium is a heavy metal that is toxic for human beings, animals and plants and is one of the most serious environmental pollutants. The International Agency for Research on Cancer (IARC) classified cadmium as a human carcinogen. Roughly 15,000 t of cadmium is produced worldwide each year for nickel-cadmium batteries, pigments, chemical stabilizers, metal coatings and alloys. Cadmium enters the organism primarily via the alimentary and respiratory tract. The sources of absorbance of this metal are foods, drinking water and air. Also a large amount of this metal is found in the wastewaters of the industrial factories.1 Additions of cadmium into the watercourses by industrial activities are different. For example, 0.1 mgL-1 for the surface treatment of metal and plastics, and 0.2 mgL-1 for the painting and electrical industry Have used.2 Therefore preconcentration and determination of trace cadmium from the natural water and wastewaters of the factories are very important and need much more attention. The traditional preconcentration and separation methods for Cd (II) are liquidliquid extraction, coprecipitation and ion-exchange, etc.3,4 These methods often require large amounts of high purity organic solvents, some of which are harmful to health and create environmental problems. Nowadays, the solid phase extraction (SPE) is being utilized for preconcentration of heavy metals and the need of more selective systems for separation of trace elements have increased the development of the synthesis of new extractants and adsorbents.1
In this study, a PVC film extraction method for the determination of trace amounts of Cd (II), based on Cd (II)-I- -MG coloring system, was developed. The Cd (II)-I- -MG complex was extracted and concentrated onto the PVC film and The absorbance of the colored membrane was measured directly by using a spectrophotometer, and the concentration of cadmium was calculated by using a calibration curve. This method offers important advantages: 1) the method is selective and free from the interferences caused by iron, zinc and copper ions in the samples. The use of PVC membrane that does not contain complexing agent is useful for selecting a suitable ligand and complexing agent which possess high sensitivity to cadmium;5 2) the method is environmentally safe since the use of toxic extraction solvents such as isobutylmethylketone, xylene and trichlorotrifluoroethan, which are employed in liquid-liquid extractions of cadmium, are eliminated;6 3) the extraction method is economical because there is no need of expensive extraction solvents;6 4) the PVC membrane does not need further treatment after it is colored and the method is simple compared to the labor and time consuming steps such as back extraction which is usually required in liquid-liquid extractions.7
EXPERIMENTAL SECTION
Apparatus. Membrane absorbance was measured by a GBC UV-VIS Cintra 20 model spectrophotometer. To adjust pH and prepare the buffer solution a JENWAY model 3510 digital pH meter was used.
Materials. All reagents were of analytical grade. Deionized water was used throughout.
Sample analysis was performed using the following chemical reagents: Bis-(2-ethylhexyl)phthalate (Merck, Germany); PVC powder(Vestolit, Germany), which consists of the K-value of 67; NaCH3COO/CH3COOH buffer solution (pH 4), which was prepared from mixing 4.7927 mL acetic acid (Merck, Germany) and 1.2633 g sodium acetate (Merck, Germany) in deionized water and diluting to the mark in a 100 mL volumetric flask; KI solution (0.9%), which was prepared by dissolving 0.9 g KI (Merck, Germany) in 99.1 g deionized water, note that 5 drops of 0.1 M Na2S2O3 (Merck, Germany) must be added to the KI solution to avoid changes in I- oxidation number; malachite green oxalate (MG) solution (0.06%), which was prepared by dissolving 0.06 g malachite green oxalate(sdFine, India) in 99.94 g deionized water; Cd (II) 100 mgL-1, which was prepared by dissolving 0.2305 g 3CdSO4. 8H2O(Merck, Germany) in a small amount of deionized water and diluting it to 1000 mL in a volumetric flask. This solution was diluted to the desired concentration when used.
Preparation of PVC membranes. 45 g bis-(2-ethylhexyl)phthalate as a plasticizer and 55 g PVC powder were placed into a beaker and was stirred with a paddle agitator. At first the paste was hard and after high-speed stirring the mixture formed a smooth paste. A small amount of the prepared paste was expanded on a flat glass surface and was heated in a 140 ℃ oven for 40 seconds. The membrane produced in this way was cut into 1×2 cm pieces, and was then ready for use.
Measurement procedure. 10 mL of aqueous sample solution containing Cd (II) and 2 mL of KI solution were placed into a glass beaker. Drops of acetic acid 1% were added to achieve pH=4. To adjust pH, 2 mL of NaCH3COO/CH3COOH buffer solution (pH=4) was added. Then 1 mL malachite green oxalate solution was added into the beaker and the mixture was diluted to the mark in a 25 mL volumetric flask with deionized water. A sheet of PVC membrane was immersed into the solution and the mixture was stirred for 25 minutes in water bath at 50 ℃. The resulting colored film was rinsed with deionized water and wiped to remove any water droplets. The same procedure was applied for standard Cd (II) solutions (25-2500 μgL-1), in order to make colored membranes. The absorbance of the colored membranes was measured 5 times at 629 nm against reagent blank film using a visible spectrophotometer. Results of the measurements and the calculated amounts of standard deviation (SD), average and relative standard deviation (RSD) are shown in Table 1. The concentration of Cd (II) was calculated from the calibration curve.
Table 1.Results of the measurements and the calculated amounts of SD, average and RSD
RESULTS AND DISCUSSION
Coloring mechanism of PVC membrane. The PVC membrane that does not contain complexing agent acts as a carrier for adsorption, extraction and concentration of the colorful complexes.3 The mechanism of formation of colorful complexes is as following:
According to this mechanism Cd (II) combines with I– into CdI42- metal complex anion. Then MG which exists in aqueous solution in the form of cationic malachite green (MG+), associates with CdI42- to form (CdI42- ).(MG+)2 ion-associated complex. This colorful ion- associated complex is extracted on PVC membrane by surface adsorption and the colored membrane is formed as a result.
Effect of KI concentration on the absorbance of the membrane. Keeping other variables constant and varying KI concentration, we studied the effect of KI concentration on the absorbance of the membrane. The absorbance was improved regularly with increasing the concentration of KI. When the concentration increased to 0.8%, the absorbance reached to a constant value (Fig. 1), and did not change with further increase in KI concentration. Thus 0.9% KI was selected to ensure that Cd (II) has completely formed CdI42- metal complex anion.
Fig. 1.Effect of KI concentration on the absorbance of the membrane.
Effect of MG concentration on the absorbance of the membrane. The effect of MG concentration on the absorbance of the membrane was studied. Fig. 2 shows that an increase in the absorbance was observed with an increase in MG concentration until 0.05%. Furthermore, the absorbance of the membrane did not change with further increase in MG concentration, which means that the whole Cd (II) in the solution has formed (CdI42- ).(MG+)2 ion-associated complexe. Hence, the use of 0.06% MG was recommended as an optimum concentration.
Fig. 2.Effect of MG concentration on the absorbance of the membrane.
Effect of pH on the absorbance of the membrane. A study of the relationship between the absorbance of the colored membrane and pH was conducted. The results showed that the most suitable pH is 4 (Fig. 3). It seems that it is the most appropriate pH for the Cd (II) to combine with I- into metal complex anion. Note that the pH should not rise above 7 because cadmium hydroxide precipitates at high pH values and less ion-associated complex is formed and consequently a decrease in the extraction of Cd (II) will occur.
Fig. 3.Effect of pH on the absorbance film of the membrane. on the absorbance.
Effect of plasticizer content of the PVC film on the absorbance of the membrane. PVC films with different plasticizer contents were made and the effect of plasticizer content of the film on the extraction of the colorful cadmium complex was studied. The absorbance of the colored membranes was measured at 629 nm by a visible spectrophotometer (Fig. 4). Although the extraction rate of colorful complex increases with increase of plasticizer content, the films become softer because they contain more plasticizer and thus are difficult to handle. The most effective film is one which contains about 45% plasticizer.
Fig. 4.Effect of plasticizer content of the film of the membrane.
Effect of temperature and stirring time on the absorbance of the membrane. The effect of temperature and stirring time were also investigated. The experiments showed that the most suitable temperature of the water bath was 50 ℃ and in higher temperatures a decrease in the absorbance of the membrane was observed (Fig. 5). It is likely that complex decomposes in temperatures above 50 ℃.
Fig. 5.Effect of temperature of water bath on the absorbance of the membrane.
The study of the stirring time showed a distinct improvement in the absorbance with increase in stirring time (Fig. 6). Over 20 minutes the absorbance reached to a constant value and did not change with prolongation of stirring time. Therefore 25 minutes was selected as the best reaction time.
Fig. 6.Effect of stirring time on the absorbance of the membrane.
Calibration curve. Fig. 7 shows the calibration curve of absorbance at 629 nm (due to the (CdI42- ). (MG+)2 complex) as a function of Cd (II) concentration. The curve is linear over the Cd (II) concentration of 10-760 μgL-1 and is expressed by the linear equation: A=0.0005C+0.0073, where A is the absorbance of the membrane and C is the concentration of Cd (II) in μgL-1 in the colorful test solution.e linear correlation coefficient, γ, is 0.9986.
In order to calculate the detection limit, the absorbance of the reagent blank film was measured 5 times at 629 nm using a visible spectrophotometer (Table 2) and the detection limit of 1.8199 μgL-1 was obtained according to the equation1.
Table 2.Measurement data for calculating the detection limit
Fig. 7.Representative calibration graph of cadmium ion concentration.
Effect of foreign ions. The effect of foreign ions was studied with the intention of applying this method to determine the concentration of trace amounts of Cd (II) in samples. 10 mL of 500 μgL-1 Cd (II) solution has put into a 25 mL volumetric flask and 2.5 mL of interfering ion with the concentration of 106 μgL-1 was added and the procedure was done (final volume is 25 mL) and the absorbance of the membrane was measured at 629 nm. The relative measurement error was calculated according to equation 2, where xt is the absorbance of the membrane in presence of Cd (II) without any interfering ion and is equal to 0.0978 according to the measurements. As it is shown in Table 3, the relative measurement error is less than 5% even in presence of high concentrations of foreign ions.
Table 3.Measured absorbances in presence of interfering ions and relative standard errors
Applications. The proposed method has been applied successfully to the determination of Cd (II) concentration in the Tadjan River’s water (Sari-Iran). 10 mL of river water was poured into a glass beaker and 2 mL KI solution was added. In addition, acetic acid 1% was added drop wise to achieve pH = 4 and then the pH were adjusted at 4 by adding 2 mL buffer solution. 1 mL malachite green oxalate solution was added into the beaker and the mixture was diluted with deionized water to the mark in a 25 ml volumetric flask. A sheet of PVC membrane was placed into this colorful test solution and the mixture was stirred for 25 min in water bath at 50 ℃. The colored membrane was rinsed with deionized water and wiped. The absorbance of the membrane was measured 5 times using the spectrophotometer at 629 nm. The results of the analysis are shown in Table 4.
Table 4.Determination of cadmium ion concentration in the Tadjan river water sample (Sari- Iran)
The concentration of Cd (II) in the colorful test solution is 11.48 μgL-1 according to the calibration curve. Note that 10 mL of the river water sample was used and the total volume of the colorful test solution was 25 mL after adding KI, buffer, MG solutions and deionized water. Thus the concentration of Cd (II) in the river water sample is 28.7 μgL-1 according to equation 3, where V1 is the total volume of the colorful test solution (25 ml); C1 is the Cd (II) concentration in the colorful test solution (11.48 μgL-1); Vx is the volume of the river water sample (10 mL) and Cx is the concentration of Cd (II) in the river water sample.
CONCLUSION
A polymeric PVC membrane has been used as the solid phase adsorbent for extraction and determination of trace amounts of Cd (II) in aqueous solutions. The preparation of the solid adsorbent is very simple and the colored PVC membrane can be kept for a few weeks without any change in the extracted species. The procedure has the advantage of avoiding organic solvents during the extraction step. No preconcentration and elution step is required and the experimental procedure is easy to carry out. Simplicity, high speed and freedom from interference have made this method suitable for the determination of cadmium in river water samples.
References
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