American Journal of Analytical Chemistry
Vol.06 No.01(2015), Article ID:53055,10 pages

Concurrent Removal and Reduction of Cr(VI) by Wool: Short and Long Term Equilibration Studies

Fawwaz H. Jumean1*, Mustafa I. Khamis1,2, Ziad A. Sara1, Mahmoud S. AbouRich1

1Department of Biology, Chemistry and Environmental Sciences, American University of Sharjah, Sharjah, United Arab Emirates

2Department of Chemistry and Chemical Technology, Faculty of Science & Technology, Al-Quds University, East Jerusalem, Palestine

Email: *

Copyright © 2015 by authors and Scientific Research Publishing Inc.

This work is licensed under the Creative Commons Attribution International License (CC BY).

Received 19 October 2014; revised 5 December 2014; accepted 23 December 2014


Hexavalent chromium removal from wastewater using sheep wool was investigated at several equilibration periods. The influence of contact time, pH, adsorbent dosage and initial concentration was investigated. Adsorption isotherms for long and short periods were fitted to the Langmuir and Freundlich isotherms. For short contact times, the Langmuir adsorption isotherm was obeyed with no detectable change in the oxidation state but removal percentages did not exceed 90%. Long contact times resulted in more than 99% removal of Cr(VI). A 2-step mechanism for the removal is proposed. Free wool and wool loaded with Cr(VI) were characterized by FTIR and SEM.


Chromium, Wool, Speciation, Adsorption Isotherms

1. Introduction

Chromium can exist in various valence states ranging from Cr(II) to Cr(VI), the most stable forms being Cr(III) and Cr(VI) [1] -[3] . These two forms exhibit large differences in physicochemical properties as well as chemical and biochemical reactivity [2] [3] . Cr(III) is relatively insoluble in water and is an essential micronutrient, whereas Cr(VI) is water soluble and is a primary contaminant due to its toxicity to humans, animal, plants and microorganisms and could also be carcinogenic [3] [4] . Chromium has widespread industrial applications that span the pharmaceutical industry, mining, leather tanning, textile dying, electroplating, aluminum conversion, coating operations, inorganic pigments industry, and wood preservatives [3] [5] . This pervasive use results in the discharge of large quantities of chromium into the environment. Accordingly, environmental scientists are paying increasing attention to reducing chromium levels in wastewater. A variety of methods have been adapted for removal of Cr(VI) from wastewater. These include reduction followed by chemical precipitation [6] , ion exchange [7] , reduction [8] , adsorption [9] , electrochemical precipitation [10] , solvent extraction [11] , membrane separation [12] , cementation [13] , evaporation, reverse osmosis, foam separation, freeze separation, and biosorption [14] .

Adsorption is an effective and versatile method for removing Cr(VI). Several publications report on the use of low cost and locally abundant adsorbents such as activated carbon [15] , agricultural byproducts [16] , waste materials [17] , and minerals [18] .

In our laboratory, we have compared the effectiveness of several low cost adsorbents in removing Cr(VI) from industrial wastewater. These include sheep wool, olive cake, sawdust, pine needles, almond shells, cactus leaves and charcoal, and have reported that wool was the most efficient adsorbent for speciation and removal of Cr(VI) [3] . However, in that study, batch mode adsorption isotherms revealed that at the optimum conditions, total chromium removal never exceeded 90% after 3-hour equilibration. In this work, we propose an efficient and low cost method that yields complete removal of Cr(VI) from wastewater while partially converting it to the essential micronutrient Cr(III). Several reports in the literature conclude that natural adsorbents [15] [16] [20] , micelle-clay complexes [21] and polymeric materials [22] can reduce Cr(VI) to Cr(III). Speciation between Cr(VI) and Cr(III) can be achieved by a combination of spectrophotometric [23] and inductively coupled plasma (ICP) measurements. The effect of pH, contact time, and particle size is studied and explained in terms of the capacity of wool to adsorb and reduce Cr(VI) to Cr(III).

2. Experimental

2.1. Chemicals

All primary chemicals used were of analytical reagent grade. Potassium chromate (K2CrO4) and chromium (III) chloride hexahydrate (CrCl3・6H2O) were purchased from Riedel De-Haen. Sodium hydroxide, hydrochloric, sulfuric, and nitric acids were purchased from Paneac. 1,5 di-phenyl carbazide, and acetone were obtained from Sigma Aldrich. The wool was washed with water and detergent for two days. The adsorbent used in the study was sheep wool, freshly trimmed from sheep in the Sharjah animal market. It was carefully cleaned, riffled, separated from impurities then air-dried. It was finally sized into 2-cm long fibers and placed in a sealed container labelled “original wool”. A portion of this wool was freeze-dried in liquid nitrogen for 10 min and then milled. Powder below 0.60 mm (mesh 30) was labelled “powdered wool”.

2.2. Instrumentation

Total chromium was determined using Varian Liberty axial sequential inductively coupled plasma-atomic emission spectrometer (ICP-AES, Varian, Australia). Cr (VI) concentrations were determined spectrophotometrically using Cary a 50 spectrophotometer (Varian, Australia). IR spectra were recorded using Spectrum One FTIR spectrometer (Perkin Elmer, USA). pH was measured by Thermo-Orion 210A+ pH meter (USA) using a combined glass electrode calibrated with buffers of pH 4.0, 7.0, and 10.0. Solutions were shaken using Edmund Buhler KS-15/TH-15 shaker (Germany) and their temperature was maintained at 25.0˚ ± 0.1˚. Scanning electron microscopy (SEM) was performed on a Tescan VEGA III LMU (Czech Republic). Electron dispersive x-ray spectroscopy (EDS) was recorded on Oxford Instruments INCA XMAX (UK).

2.3. Methods

Stock solutions containing 500 ppm Cr(VI) were prepared by dissolving potassium dichromate in deionized water. Standard solutions of 10, 20, 50, 100, 150 & 200 ppm were prepared by dilution. Stock ligand solutions were prepared by dissolving 1,5 diphenyl carbazide in acetone.

Batch adsorption studies were carried out in flasks containing 100 ml of test solutions at the desired initial chromium concentrations. pH was adjusted using either 0.10 M HCl or 0.10 M NaOH. Wool was then placed in the flasks and the contents shaken for 3-h at 25.0˚C and 150 rpm. At known equilibration times, aliquots were withdrawn and analyzed for total chromium and Cr(VI).

Spectrophotometry was used to determine Cr(VI) concentrations using 1,5 di-phenyl carbazide. A 0.10 ml aliquot was collected and mixed with 0.20 ml of this ligand and 2 drops of 6.0 M sulfuric acid and the volume adjusted to 10 ml. The Cr(VI)-ligand complex was allowed to equilibrate for 10 min before measuring its absorbance at 540 nm [22] . ICP was used to determine total chromium in samples and standards using the method provided by the manufacturer.

3. Results and Discussion

3.1. Effect of Contact Time

Figure 1 shows the effect of contact time in the short term mode (0 - 3 h). The data reveal no dicsernible effect of particle size (original vs. powdered wool) on Cr(VI) removal efficiency. Furthermore, there is no apparent distinction between Cr(VI) and total chromium concentrations, indicating that Cr(VI) is virtually the only species present The maximum removal efficiency is ca 88%, in conformity with our previous findings [5] [6] .

Figure 2 shows the effect of contact time on Cr(VI) removal in the long term mode (0 - 165 h). For both wool forms Cr(VI) was almost totally removed from solution after 100 h. However, the total chromium concentration at pH 1.5 decreased by 90% up to 120 h equilibration before rising at higher times. The increase in Cr(III) concentration with time is indicative of removal of Cr(VI) by wool, followed by reduction to Cr(III) and subsequent release of Cr(III) into solution. The sequence is further supported by FTIR data (see below). Control experiments in absence of wool indicate that Cr(VI) is relatively stable in both time modes.

3.2. Effect of pH

The effect of pH on chromium removal efficiency is shown in Table 1 for the long term mode for the pH range 1.5 - 6.0, from which it can be deduced that removal is favored by high acidity. This can be seen in Figure 2 which shows results at pH 1.5 and pH 2.0.

On the other hand, short term mode studies (2-h contact time) showed no difference in removal at pH 1.5 and 2.0. Table 1 also shows that the percent removal of Cr(VI) is much larger than that of total chromium, indicating speciation between Cr(VI) and Cr(III) [23] [24] . The acid catalyzed reduction of Cr(VI) to Cr(III) on wool may be represented by


This mechanism is similar to that proposed in previous reports [20] [24] [25] for removal of Cr(VI) by other natural adsorbents. Table 1 shows the optimum pH for the removal of Cr(VI) by original wool is 1.5.

Figure 1. Variation of total Cr and Cr(VI) concentrations with time using original and powdered wool as adsorbents in the short term mode. Adsorbent dosage = 8.0 g/L, pH = 2.0 and T = 25.0˚C, shaking speed = 150 rpm.

Figure 2. Changes in total chromium and Cr(VI) concentrations as a result of equilibration with wool in the long term mode. Adsorbent dosage = 8.0 g/L, pH = 1.5 and 2.0, T = 25.0˚C, shaking speed = 150 rpm. Top two curves are control experiments in absence of wool.

Table 1. Percent removal of total chromium and Cr(VI) by original and powdered wools as a function of pH in the long term mode (5 days). Adsorbent dosage = 8.0 g/L, T = 25.0˚C, shaking speed = 150 rpm. Concentrations are in ppm.

3.3. Effect of Wool Dosage

Figure 3 summarizes the effect of wool dosage on removal of Cr(VI) and total chromium at pH = 2.0, for a 5-day contact time. The data show that the optimum dosage of wool is 8.0 g/L. Figure 3 also reveals that the extent of reduction of Cr(VI) in the long term mode is enhanced by higher dosages. Whereas Cr(VI) removal at dosages higher than 8.0 g/L remains constant, total chromium removal is hindered by high dosages. This result may be explained by positing that high dosages serve to increase the rate of reduction of Cr(VI) to Cr(III), followed by release of Cr(III) into solution.

Figure 3. Variation of percent removal of total chromium and Cr(VI) with adsorbent dosage using original wool as adsorbent in long term contact time mode. Initial concentration of Cr(VI) = 100 ppm, pH = 2.0, T = 25.0˚C, shaking speed = 150 rpm.

3.4. Adsorption Isotherms

Adsorption data were fitted to the Langmuir (Equation (2)) and Freundlich (Equation (3)) isotherms [3] .



where Ce is the equilibrium concentration of total chromium (mg/L), qe is the amount adsorbed at equilibrium, in mg/g adsorbent. Q (mg/g) and b (L/mg) are the Langmuir constants, representing adsorption capacity and energy, respectively. Kf and n are the Freundlich constants.

Figure 4 gives the variation of q with the equilibrium concentration of Cr(VI) in the long term contact time mode. The data reveal that q follows the same pattern at pH 1.5 and 2.0, the asymptotic trend indicating a monolayer. The Langmuir isotherm gives a good fit for the data (Figure 5). However, the dependence of the term Ce/qe on equilibrium concentration in the long term mode does not obey this isotherm, indicating that calculations based on total chromium in solution cannot be attributed to Cr(VI) alone. Thus speciation of chromium takes place, with release of Cr(III) into solution following reduction of adsorbed Cr(VI). This finding demonstrates the efficacy of species resolved techniques in the study of adsorption isotherms for this type of complex system. By contrast, an earlier study using short term equilibration (2-h contact time) revealed that adsorption data for total chromium obeyed the Langmuir isotherm [3] . For this mode both Cr(VI) and total chromium fit this isotherm (Figure 6). These results may be explained by a two-step mechanism. The first is adsorption on wool accompanied by rapid equilibrium, and the second is a slow reduction of Cr(VI) to Cr(III), followed by release of Cr(III) into solution. Results for the short term mode reflected primarily the fast first step.

Figure 5 and Figure 6 yield the Langmuir parameters for short and long term modes. Table 2 summarizes the results for total chromium and Cr(VI) and shows that Q is larger for Cr(VI) in the long term mode and is also larger than that for total chromium in both modes. This indicates that in long term mode, more sites are available for Cr(VI) than in short term mode. This finding may be explained by postulating that some sites occupied by Cr(VI) undergo simultaneous reduction and release of Cr(III) to the solution.

Table 3 summarizes the fit of the data to the Freundlich isotherm Inspection of this table reveals that the correlation coefficient for both Cr(VI) and total chromium in the short term mode is smaller than that for Langmuir isotherm (Table 2). By contrast, for the long term mode, total chromium data obey the Freundlich, but not the Langmuir, isotherm. This indicates the non-ideality of total chromium adsorption which in turn may be attributed to the proposed mechanism above. Upon comparing the maximum adsorption capacity (Q) obtained under long term equilibration with values previously reported for low cost adsorbents [21] [22] [26] -[30] , the value obtained in this work is among the highest 5%.

Previously reported data on the elution profile of Cr(VI) from columns packed with wool [19] had been based solely on ICP, which measures total chromium. The authors had assumed that all Cr(VI) is retained after passing through the column, and had not considered the possibility of reduction to Cr(III). Reduction may indeed not

Figure 4. Amount of chromium removed in mg/g (q) by trimmed original wool as function of Ce, the equilibrium concentration of Cr(VI). Adsorbent dosage = 8.0 g/L, T = 25.0˚C, shaking speed = 150 rpm.

Figure 5. Langmuir isotherm for Cr(VI) and total chromium using original wool as adsorbent in long term mode (5 days). Adsorbent dosage = 8.0 g/L, pH = 1.5, T = 25.0˚C, shaking speed = 150 rpm.

Figure 6. Langmuir isotherm for Cr(VI) and total chromium using original wool as adsorbent in short term mode (contact time 3 h). Adsorbent dosage = 8.0 g/L, pH =1.5, T = 25.0˚C, shaking speed =150 rpm.

Table 2. Langmuir parameters (b, Q and R2) for total chromium and Cr(VI) for short term and long term equilibration periods, with original wool as adsorbent. Adsorbent dosage = 8.0 g/L, T = 25.0˚C, shaking speed =150 rpm.

Table 3. Freundlich isotherm parameters (Kf, n and R2) for total chromium and Cr(VI) for short and long term modes using trimmed wool as adsorbent. Adsorbent dosage = 8.0 g/L, T = 25.0˚C, shaking speed =150 rpm.

occur when the contact time between wool and the eluent is very short. Under such conditions, all forms of chromium are essentially removed. However, when solutions containing Cr(VI) were left in contact with wool in the column for longer periods, the first fraction contained higher concentrations of total chromium, and this can now be attributed to the presence of Cr(III). To verify this conclusion, 100 ppm Cr(VI) solution was applied to a column packed with original wool and eluted at a constant rate of 2.0 ml/min. 100 ml fractions of eluents, representing short term equilibration were collected for four successive overnight periods, with the elution stopped at the end of each day, thereby allowing long term equilibration of Cr(VI) on wool. The data for total chromium and Cr(VI) are presented in Figure 7. Virtually, the only form of chromium eluted overnight is Cr(III). This corroborates the finding that upon prolonged exposure on wool, Cr(VI) undergoes reduction to Cr(III).

3.5. FTIR Spectroscopy

Figure 8 displays FTIR spectra of wool before and after adsorption of Cr(VI). The very weak peak at 939 cm1 in free wool becomes much more pronounced in wool loaded with chromium for long term contact, due to the oxidation of wool by Cr(VI). This peak can be attributed to S=O bonds that form when cystine in wool is oxidized. A similar assignment has been reported for wool oxidized by UV irradiation [31] . This finding supports the proposed mechanism for removal of Cr(VI) by wool from aqueous solution (Equation (1)).

3.6. Electron Dispersive X-Ray Spectroscopy (EDS)

Scanning electron microscopy (SEM) was employed to study the surface of wool before and after loading with chromium. In order to obtain the elemental analysis of the surface, EDS spectra were recorded for both samples (Figure 9). Inspection of this figure reveals that chromium is retained on wool at the end of the long term contact time, with the appearance of a chloride peak from HCl.

Figure 7. Mass of chromium species in eluted fractions. Fraction volume = 100 ml, total applied volume = 2.5 L, pH of applied solution = 1.5, wool mass 26.0 g, wool depth = 29.0 cm. T = 25.0˚C.

Figure 8. FTIR spectra of free wool (bottom) and wool loaded with ionic chromium species (top).

Figure 9. EDS results for original free wool (top) and wool loaded with ionic chromium species (bottom).

4. Conclusion

The affinity of wool for Cr(VI) varies with contact time and pH. For short contact times, the Langmuir adsorption isotherm was obeyed with no detectable change in the oxidation state. However, removal percentages did not exceed 90%. Long contact times resulted in more than 99% removal of Cr(VI). A 2-step mechanism for this removal is proposed. The first involves fast adsorption of Cr(VI) on wool and the second a slow catalytic reduction of Cr(VI) to Cr(III), followed by desorption of Cr(III) into solution. The surface of wool before and after adsorption was characterized by FTIR and EDS and the results with the suggested mechanism. The optimum parameters for this significant improvement in Cr(VI) removal and hence its environmental remediation can now be identified as pH 1.5, contact time of at least 5 days, and a minimum adsorbent dosage of 8.0 g/L. For the short term study, pH 2.0 was selected so as to provide comparison with previous results. Cr(VI) adsorption follows the Langmuir adsorption isotherm with Q = 64.5. This high capacity of wool for Cr(VI) provides a practical solution for the removal of Cr(VI) from industrial wastewater. A plant can be constructed consisting of a batch adsorption reactor with a 5-day retention time in which Cr(VI) is mostly removed. The effluent could then subjected to pH 10.0 at which Cr(III) precipitates as hydroxide which can be recovered by sand filtration for further reuse.


This research was supported by the American University of Sharjah, Grant FRG12-2-10.


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