Polystyrene tris(2-aminoethyl)amine, Potassium dichromate, 1,5-Diphenyl carbazide, sodium hydroxide, and sulfuric acid were purchased from Sigma-Aldrich (Israel) and were used as received. All solutions were prepared in deionized distilled water. Cr (VI) stock solution (1000 mg/L) was prepared by dissolving the appropriate amount of K₂Cr₂O₇ in deionized distilled water. This solution was diluted as required to obtain 5.0 - 80 mg/L Cr (VI) standard solutions. The batch experiments were carried out in 100 ml Erlenmeyer flasks by agitating a pre-weighed amount of the polymer with 50 ml of the aqueous Cr (VI) solution at 25˚C ± 1˚C. The initial pH of the solution was adjusted using 0.2 N H₂SO₄. A muli-element standard solution (51844) for calibration of the ICP-MS was obtained from Sigma-Aldrich (Israel).

The concentration of Cr (VI) was determined colorimetrically using a Perkin-Elmer Lambda 5 UV-Visible spectrophotometer and the total Chromium concentration was determined using inductively coupled plasma-mass spectrometer (ICP-MS, Agilent Technologies 7500 Series). A calibration curve for Cr (VI) was obtained by plotting the absorbance of Cr (VI) solutions of different concentrations after complexation with the 1,5-di- phenyl carbazide ligand at 540 nm. The curve was linear within the selected Cr (VI) concentrations with a correlation coefficient (R²) of 0.9996. While a second calibration curve for total Cr was prepared by analyzing the standard solutions prepared from a multi-element standard solution by ICP-MS. The curve was linear through the selected concentrations with a correlation coefficient (R²) of 0.9987.

The adsorbent dosage was varied in the range of 2.00 and 30.0 g/L with initial Cr (VI) concentration of 10.0 mg/L. Samples were analyzed for total Cr (ICP) and Cr (VI) (UV-Vis) concentrations after a contact time of 180 minutes and at pH = 5.0.

Scanning electron microscopy (SEM) and (EDS) analyses of the adsorbent before and after complexation with chromium ions were recorded on JEOL model, JSM-5410 LV-country. The samples were mounted on metal stubs and then coated with gold (Polaron Spatter coater). The images were taken with an accelerating voltage of 25 kV, at high vacuum (HV mode) and secondary electron image (SEI). The analysis was done using Oxford systems-Liquid Nitrogen cooled solid state Energy Dispersive Spectrometer detector and link ISIS software.

Regeneration of the polystyrene tris(2-aminoethyl)amine was performed by mixing the chromium-chelated adsorbent with 1 M KCl aqueous solution and then agitated for 2 hours. The regenerated adsorbent was tested by agitating it with 10 ppm Cr (VI) solution for 2 hours and the percent removal was calculated by determining the initial and the final concentration of Cr (VI) in the solution using the colorimetric method.

Figure 1 and Figure 2 summarize the effect of adsorbent dosage on the percent removal of Cr (VI) and total Cr, respectively. Inspection of these figures reveals that the percent removal of Cr (VI) and of total Cr increased with increasing adsorbent dosage and attained a constant value after a dosage of 10 g/L. Hence the optimum dosage for the removal of Cr (VI) by polystyrene tris(2-aminoethyl)amine was set at 10.0 g/L.

The effect of contact time on the percent removal of Cr (VI) and on the concentration of total Cr by polystyrene tris-(2-aminoethyl)amine with the optimum dosage of 10 g/L is demonstrated in Figure 3 and Figure 4. The

percent removal as measured by Cr (VI) and by total Cr increased with increasing contact time and attained equilibrium at 120 minutes. These results revealed that 120 minutes was the optimum contact time needed to attain equilibrium. Therefore, in all subsequent measurements, the adsorption contact time was set at 120 minutes.

Figure 5 displays the effect of contact time on the emergence of Cr (III) in solution. It is evident that the concentration of Cr (III) in solution passes through an induction period, an adsorption period and a saturation period. It took 20 min for Cr (III) to build up in solution. Once accumulated, it is removed by adsorption on the polymer until it reached saturation. This explains the observed fluctuation in its concentration as function of time.

The percent removal of Cr (VI) was studied at different pH values ranging between 2.0 - 6.0 (Figure 6). Whereas the percent removal of Cr (VI) stayed almost constant as the pH was increased, that of the total Cr was found to vary significantly with pH (Figure 7). This led to the conclusion that the difference was due to the emergence of Cr (III) ions in the solution. Apparently some of the bound Cr (VI) ions were reduced by the adsorbent to Cr (III) ions. The concentration of the latter was determined as the difference between the total chromium obtained by ICP-MS and Cr (VI) obtained by UV-Vis spectroscopy. Inspection of Figure 7 reveals that at

pH = 2 the concentration of Cr (III) available in solution was about 7 ppm, then it dropped significantly when the pH was raised. It is known that the reduction of Cr (VI) to Cr (III) is also catalyzed by H⁺ [10] [11] . Hence the rate of reduction is much higher at pH = 2 than that at pH 6, leading to the observed increase in [Cr (III)] at pH = 2.

In agreement with previously reported results [10] [11] , two mechanisms appear to be involved in the removal of Cr (VI) by polystyrene tris-2-(aminoethyl) amine; adsorption and reduction. So the removal can be performed by any of the two processes. If the intention is to remove Cr (VI), then pH = 6 should be chosen. While if the intention is to detoxify Cr (VI), then the redox process is the preferred route and this should be performed at pH = 2.

The effect of initial Cr (VI) concentration on the percent removal of Chromium was studied over the range 10.0 to 80.0 mg/L at the optimum contact time of 120 minutes, pH = 5.0 and at an adsorbent dosage of 10 g/L (Figure 8). The results obtained by UV-Visible and by ICP-MS, indicated that the percent removal of Cr (VI) decreased with increasing initial concentration.

The scanning electron microscope images (Figure 9) showed an increase in average particle size from 71 µm (polystyrene tris(2-aminoethyl)amine alone) to 88 µm (polystyrene tris(2-aminoethyl)amine bound to Cr (VI)), this increase in average particle size is caused by the complexation of Cr (VI) to the polymer.

Elemental analysis using Energy Dispersive Spectrometry showed the appearance of Cr after the complexation of polystyrene tris(2-aminoethyl)amine with Cr (VI) ions. The appearance of S is attributed to the use of sulfuric acid in pH adjustment (Table 1 and Table 2).

The concentration of Cr (VI) desorbed was 0.27 ppm while the total chromium found in the solution was 4.13 ppm. The difference (3.85 ppm) represented the concentration of Cr (III) exchanged by KCl solution. Hence, we can conclude that the adsorbent reduced almost all the bound Cr (VI) to Cr (III). The percent desorption was calculated using the initial concentration of Cr (VI) on the adsorbent and the final concentration of Cr (III) and Cr (VI) in KCl solution and was found to be 89.3%.

The percent removal of Cr (VI) by the regenerated adsorbent was 95.11%. The removal capacity of the latter adsorbent was comparable to that of the original polymer which was 96.74%. This demonstrates the high efficiency of KCl in desorbing chromium from polystyrene tris(2-aminoethyl)amine.

To model the adsorption behavior, two adsorption isotherms were studied and their correlation with the experimental data was assessed.

Apparently, the adsorption mechanism initially starts with an electrostatic attraction between the ammonium ions, generated at acidic pH from the amino groups attached to the polymer, with the predominant chromium

species, [16] . This is followed by reduction to Cr (III) and complex formation with the four amino groups situated on the polymer [23] [24] . The adsorbent itself being oxidized to the N-oxide as apparent from the IR spectrum that shows a small band at about 940 cm⁻¹ corresponding to the N-O stretching vibration. Also the bands in the region 1100 - 800 cm⁻¹ corresponding to C-N stretching vibrations have shifted to lower frequencies indicating complexation of the polymer with chromium (Figure 13). The generated Cr (III) was either released to the aqueous phase or adsorbed depending on the availability of free sites. Upon addition of 1 M KCl to the adsorbent, Cr (III) was released to the solution and was determined by ICPMS (Figure 14).

The adsorption capacity of the polystyrene tris(2-aminoethyl)amine under ambient pH and at 25˚C was found to be 312.27 mg/g of adsorbent. This is about five times more than the most efficient adsorbent reported earlier, particularly, Neem sawdust and cationized cellulose (Table 3). The acceptable cost and the efficiency of our adsorbent makes it a good candidate for the removal of Cr (VI) from aqueous media.