Noorbasha N.
Meeravali
,
K.
Madhavi
and
Sunil Jai
Kumar
*
National Center for Compositional Characterization of Materials (NCCCM), Bhabha Atomic Research Centre, ECIL Post, Hyderabad, 500 062, India
First published on 5th November 2010
A highly sensitive and novel sequential non-chromatographic speciation procedure has been developed for selective pre-concentration and separation of Cr(III) and Cr(VI) from natural and wastewaters. In this procedure, Triton X-114 micelle and cetylpyridinium bromide-Triton X-114 mixed-micelle are used sequentially for the extraction of hydrophobic Cr(III)-trifluoropentanedione and hydrophilic Cr(VI), respectively. Inductively couple plasma optical emission spectrometry (ICP-OES) is used for its determination. The parameters affecting the extraction process are optimized. Under the optimized conditions, the pre-concentration factors obtained are 50 and 15 while limits of detection (LOD) are 0.02 and 0.05 ng mL−1 for Cr(III) and Cr(VI), respectively. These LODs are better than those of IC-ICP-MS and comparable to those of IC-ICP-DRC-MS methods. The recoveries are in the range of 95 to 99% at 10 to 40 ng mL−1 with relative standard deviation of 2–4%. The accuracy of the procedure is validated by comparing the sum of the concentrations of each individual chromium species obtained from sequential extraction with total chromium in BCR certified reference materials such as Effluent-713, Influent-714 and Industrial effluent-715. The method was then applied to various water samples collected locally.
Over the decades, ion chromatographic (IC) separation followed by post column diphenylcarbazide (DPC) spectrophotometer detection has been the most widely used differential speciation approach for the determination of Cr(VI) and total chromium after oxidation of Cr(III). The separation of Cr(VI) has been achieved by either anionic or cationic exchangers.6–9 The main difficulty observed in these procedures is overloading of the columns with high levels of anionic and cationic species present in the sample and effect of dissolved organics that prevents Cr(VI) reaction with DPC. Recently, the combination of IC with inductively coupled plasma mass spectrometry detection is more frequently used simultaneous speciation approach for the determination of both the species Cr(III) and Cr(VI). The main drawbacks of this approach are isobaric interferences due to chloride and organic content if present in the sample, high instrumental operation time, and high cost make it difficult to facilitate these procedures in routine analysis. In some natural water samples the level of these species are below the limits of detection of these methods.10–12 To alleviate these problems, simultaneous matrix separation and pre-concentration procedure is an effective alternative, hence, non-chromatographic speciation procedures such as solid phase micro extraction and cloud point extraction are being developed.13,14 These are simple, fast and cheaper methods that provide high pre-concentration, which facilitates the use of even ICP-OES for the determination.
At present various cloud point extraction (CPE) procedures have been reported for speciation of chromium using differential approach.15–24 The differential approach often yields highly imprecise values, especially when the concentration of one species is far higher than the other. Therefore a method where both the species are determined sequentially is desirable.
In this paper, for the first time, we describe a novel sequential micelle and mixed-micelles cloud point extraction procedure for the separation and pre-concentration of Cr(III) and Cr(VI) from natural and wastewaters using ICP-OES. Triton X-114 micelles are used for selective extraction of Cr(III)-trifluoropentanedione (TFPD) in the presence of Cr(VI). The supernatant containing Cr(VI) is subjected to similar extraction produce after addition of cetylpyridinium bromide CPB-Triton X-114 mixed-micelle. The accuracy of the procedure is verified by analyzing the BCR certified reference materials such as Effluent-713, Influent-714 and Industrial effluent-715.
ICP-OES instrument | JY-2000 |
Rf power/W | 1000 |
Plasma gas flow/L min−1 | 12 |
Auxiliary gas flow/L min−1 | 1.1 |
Nebulizer gas flow/L min−1 | 0.5 |
Slit width/μm | 20/20 |
Wavelength/nm | 267.7 |
Monochromator/m | 0.64 |
Number of groves/mm | 2400 |
Type of monochromator | Czerny Turner |
Fig. 1 Mixed-micelles CPT of 1% m/v Triton X-114 micelles with CPB monomer (<CMC) and micelles (>CMC) with and without 1% v/v NH4SCN in presence of 1% v/v HCl. |
The effect of pH on the sequential micelles and mixed-micelles separation and pre-concentration of Cr(III) and Cr(IV) was investigated. Hence, the effect of pH in the range of 1–6 on the recovery of Cr(III) and Cr(VI) were studied. Results are shown in Fig. 2. As can be seen in Fig. 2(a), in the pH range of 4.2–6.0, the recovery of Cr(III)-TFPD was 98–102%, whereas only 4–5% recovery of Cr(VI) was observed at the whole pH range studied using the micelles extraction system. Thus, pH 5 was selected for selective extraction of Cr(III)-TFPD in presence of Cr(VI). As can be seen in Fig. 2(b), in the pH range 1.5–3.5, the recovery of Cr(VI) was 92–96%, and then decreased to 40% on further increase in pH of the solution to 6, whereas only 5–6% recovery of Cr(III) was observed in the whole studied pH range under these conditions. Thus, pH 2.5 was used for selective extraction of Cr(VI) in the presence of Cr(III), by using mixed-micelles in the presence of NH4SCN.
Fig. 2 Effect of pH on the recovery of Cr(III) and Cr(VI) using sequential (a) micelles (in presence of 0.3% m/v TFPD and 0.3% m/v Triton X-114) and (b) mixed-micelle (in presence of 0.3% m/v CPB, 0.8% m/v of Triton X-114 and 0.6% v/v NH4SCN). The error bar indicates the standard deviation at each measurement (n = 3). |
Optimizations of concentration of chelating agents such as TFPD for Cr(III) and CPB for Cr(VI) are necessary especially in wastewater samples for quantitative extraction using micelle and mixed-micelle, respectively. The preliminary results indicated that the concentration of TFPD and CPB required for quantitative extraction of chromium species from aqueous solution was quite different compared to real wastewater sample. Therefore, the effect of the concentrations of TFPD and CPB on the recovery of Cr(III) and Cr(VI) spiked aqueous solutions and wastewaters were evaluated carefully in the concentration range of 0–0.5% m/v. The results showed that 100 and 96% recovery of Cr(III) and 94 and 92% recovery of Cr(VI) were obtained from aqueous and wastewaters by addition of 0.08% and 0.20% TFPD, and 0.1 and 0.2% CPB, respectively. Above these concentrations of TFPD and CPB the recoveries are unchanged. The different behaviors at lower concentrations of TFPD and CTAB may be due to differences in the concentration of metal ions available to compete with chromium species reaction with chelating agents. Hence, a concentration of 0.3% m/v TFPD and 0.3% m/v CPB were selected, respectively for micelles and mixed-micelles.
Optimization of Triton X-114 concentration on the recovery of Cr(III) and Cr(VI) spiked aqueous and wastewaters were evaluated carefully in the range of 0–1% m/v. The results showed that the recovery of Cr(III)-TFPD increased with increase in concentration of Triton X-114 and reached 98 and 100% recovery at 0.1 and 0.2% respectively, in wastewater and aqueous solutions. Not much change in the Cr(III)-TFPD recovery was observed by further increase in Triton X-114 concentration up to 1%. Hence, 0.3% Triton X-114 concentration was selected. In case of mixed-micelles, clear phase separation in the supernatant solution was obtained at and above 0.4% Triton X-114 concentration added to 0.3% CPB in the presence of NH4SCN. At 0.4% Triton X-114, the recovery of Cr(VI) from aqueous and wastewaters were 60 and 75%, respectively. These recoveries increased further by increase in concentration of Triton X-114 up to 0.7 and 0.6%, respectively, for aqueous and wastewaters and reached maximum 95% recovery in both the matrices. This recovery of Cr(VI) was constant by further increasing the Triton X-114 concentration up to 1%. Hence, a 0.8% Triton X-114 concentration was selected.
As shown in Fig. 1, the NH4SCN electrolyte is playing a very important role in achieving the cloud point phase separation in CPB-Triton X-114 mixed micelles. Hence, the effect of NH4SCN on Cr(VI) recovery was studied in the range of 0 to 1.5% m/v. These results show that without electrolytes no phase separation was observed and no recovery of Cr(VI). At 0.2% NH4SCN, the surfactant-rich phase (SRP) was observed on top of aqueous solution. In between 0.2 to 0.3%, SRP was floating on the solution. On further increase in the concentration of NH4SCN to 0.4%, the SRP was settled at bottom of the solution and showed 80% recovery of Cr(VI). This recovery was reached 97% at 0.5% NH4SCN and remained constant up to 1.5%. Hence, a 0.6% m/v NH4SCN concentration was selected.
The optimization of incubation temperature and time is necessary, especially for complete complexation and quantitative extraction of inert Cr(III) and water soluble Cr(VI) species sequentially from aqueous solution into pre-concentrating micelle and mixed-micelle SRP. The volume of these SRP decides the phase volume ratio (PVR) and pre-concentration factor (PCF). The PVR is the ratio of the final volume of the SRP to that of the aqueous phase. The PCF is the ratio of the analyte concentration in the final SRP to that of the initial aqueous phase. Therefore, the effect of incubation temperature on SRP volumes and recovery of Cr(III) and Cr(VI) were studied in the range 30 to 90 °C using 30 min incubation time. The recoveries of chromium species along with corresponding SRP volumes are shown in Fig. 3. These results indicate that the extraction of reactive anionic Cr(VI) was independent of temperature in the studied range. But in the case of Cr(III), temperature is playing a very important role and the quantitative recovery (98%) was achieved only after 60 °C incubation temperature.
Fig. 3 Effect of incubation temperature on sequential micelle and mixed-micelle recovery of Cr(III) and Cr(VI) and SRP volumes. The error bars indicate the standard deviation at each measurement (n = 3). |
The incubation temperature is also playing an important role on the volume of SRP. The SRP volumes of 1000 and 100 μL were obtained for micelle and mixed-micelles respectively in the range of 30–50 °C temperature, and further increase caused decrease in the volumes of SRP and reached constant of 300 and 50 μL in between 70-90 °C. Therefore an 80 °C incubation temperature was selected and it has provided that the lowest SRP volume and quantitative recoveries. The optimization of incubation time was carried out in the range 10 to 60 min. These experiments showed that 98% and 95% recovery of Cr(III) and Cr(VI) was observed after 15 min of incubation time. Therefore, 20 min incubation time was selected. Under these conditions, the achieved PCF for Cr(III) and Cr(VI) were 50 and 15, respectively.
The recovery studies were performed after spiking BCR certified reference materials (BCR 713, 714 and 715) and wastewater samples collected locally from various industrial areas. The spiking concentrations were approximately similar to allowed concentrations of these species in natural waters, for better demonstration of the performance of the procedure. Therefore, BCR certified reference materials and wastewater samples were spiked with Cr(III) and Cr(VI) in the range 10 to 200 ng mL−1 and at different concentrations, and the recoveries were measured. As shown in Table 2, the recoveries were between 95 to 99%, which indicated that these matrices have no effect on sequential recoveries of chromium species.
Matrices | Spiked/ng mL−1 | Recovery (%) | ||
---|---|---|---|---|
Cr(III) | Cr(VI) | Cr(III) | Cr(VI) | |
a Values are means of four measurements ± standard deviation. b Not detected. | ||||
BCR-713 | 10 | 0 | 97.2 ± 2.5 | NDb |
0 | 20 | NDb | 95.8 ± 3.2 | |
10 | 20 | 96.8 ± 2.9 | 96.8 ± 3.5 | |
BCR-714 | 30 | 40 | 97.8 ± 1.9 | 97.8 ± 2.5 |
40 | 30 | 98.6 ± 2.2 | 98.2 ± 2.8 | |
BCR-715 | 100 | 200 | 99.8 ± 2.3 | 98.8 ± 1.9 |
200 | 100 | 99.6 ± 1.6 | 97.2 ± 2.8 | |
Real samples | ||||
Electronic industry | 20 | 10 | 97.6 ± 2.3 | 95.2 ± 2.8 |
Pharmaceuticals | 10 | 10 | 98.8 ± 1.9 | 94.8 ± 3.6 |
Domestic drainage | 10 | 0 | 95.6 ± 2.6 | NDb |
0 | 20 | NDb | 97.3 ± 2.9 | |
10 | 20 | 94.8 ± 2.4 | 95.8 ± 3.1 | |
20 | 10 | 98.6 ± 2.3 | 96.8 ± 3.4 |
Speciation approach | Separation scheme | Instrument | LOD/ng mL−1 | Ref. | |
---|---|---|---|---|---|
Cr(III) | Cr(VI) | ||||
a Cr(III) and total chromium using differential speciation approach. b Diphenylcarbazide. c Spectrophotometer. d Simultaneous determination of Cr(III) and Cr(VI). e Dynamic reaction cell. f Sequential determination of Cr(III) and Cr(VI). | |||||
Cr(III) & Cr (T) Da | Micelle | GFAAS | 0.021 | — | 16 |
Cr(III) & Cr (T) Da | Micelle | FAAS | 0.32 | — | 17 |
Cr(III) & Cr (T) Da | Micelle | GFAAS | — | 0.01 | 18 |
Cr(III) & Cr (T) Da | Micelle | FAAS | — | 0.6 | 20 |
Cr(VI) | IC-DPCb | SP c | — | 0.05 | 7 |
Cr(VI) | IC-DPC | SP | — | 0.018 | 9 |
Cr(III) & Cr(VI) Sd | IC | ICP-MS | 0.3 | 0.5 | 10 |
Cr(III) & Cr(VI) Sd | IC | ICP-MS | 0.2 | 0.1 | 12 |
Cr(III) & Cr(VI) Sd | IC | ICP-DRC-MS e | 0.09 | 0.06 | 28 |
Cr(III) & Cr(VI) Sqf | Micelle and mixed-micelle | ICP-OES | 0.02 | 0.05 | Present method |
Matrices | Measured values a/ng mL−1 | Certified values/ng mL−1 | |||
---|---|---|---|---|---|
Cr(III) | Cr(VI) | Total Crb | Total Crc | ||
a Mean of six determinations ± standard deviation. b Values are obtained by addition of Cr(III) and Cr(VI) values. c Values are obtained from CPE procedure with chelating agent ref. 20. d Values are in μg mL−1. | |||||
BCR-713 final effluent | 16.7 ± 1.1 | 4.9 ± 1.4 | 21.6 ± 1.8 | 21.4 ± 2.5 | 21.9 ± 2.4 |
BCR-714 initial influent | 77.4 ± 5.5 | 47.2 ± 6.2 | 126.6 ± 8.3 | 123.3 ± 4.7 | 123 ± 10 |
BCR-715 Industrial effluentd | 0.55 ± 0.05 | 0.48 ± 0.03 | 1.03 ± 0.06 | 0.99 ± 0.08 | 1.00 ± 0.09 |
Analysis of real samples | |||||
Electronic industry | 2.1 ± 0.2 | 8.2 ± 0.5 | 10.3 ± 0.5 | 10.5 ± 1.1 | — |
Pharmaceuticals | 4.4 ± 0.1 | 7.4 ± 0.4 | 11.8 ± 0.4 | 14.9 ± 0.8 | — |
Domestic drainage | 2.5 ± 0.2 | 6.8 ± 0.5 | 9.3 ± 0.5 | 10.3 ± 0.9 | — |
This journal is © The Royal Society of Chemistry 2011 |