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2. ENVIRONMENTAL ChEMISTRy & TEChNOLOGy 2.1. Lectures

2. ENVIRONMENTAL ChEMISTRy & TEChNOLOGy 2.1. Lectures

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Chem. Listy, 102, s265–s1311 (2008) Environmental Chemistry & Technology<br />

concentration range 0.5–10 g dm –3 . The results are presented<br />

in Table II. Increase of the sorbent dose in solution caused<br />

a decrease of akaganeite sorption capacity. However, this is<br />

not a good indicator of sorption ability, because with bigger<br />

sorbent concentrations all the available active sorption sites<br />

are not occupied. It is important to see what is the remaining<br />

As (V) concentration after treatment. In a real system this is<br />

the important factor; the remaining concentration should be<br />

below the limits. In the last column of Table III the remaining<br />

concentrations are given. It is observed a significant decrease<br />

of the remaining As (V) conc. with increase of the sorbent<br />

dose. It seems that a good dose is 5 g dm –3 , which gives a<br />

96 % removal and a satisfactory final As concentration of<br />

4 mg dm –3 .<br />

Table III<br />

The effect of sorbent dose<br />

C S [g dm–3 ] Q [mg g –1 ] C eq [mg dm –3 ]<br />

0.5 43.0 78.5<br />

1.0 41.4 58.6<br />

<strong>2.</strong>0 36.3 27.4<br />

5.0 19.2 4.0<br />

10.0 9.6 4.0<br />

Conclusions<br />

Synthetic akaganeite is a suitable sorbent for arsenic<br />

removal, especially at acidic environment. It is a low cost<br />

sorbent, as it is prepared from easily available cheap inorganic<br />

materials and has a good efficiency (above the average<br />

s473<br />

reported in the literature). It removes arsenic by chemical<br />

sorption favored by an increase of temperature and the best<br />

results are obtained at pH 3.5. However, at pH 7.0, gives<br />

also satisfactory results. This is important for the treatment<br />

of drinking water. The capacity of the material was not affected<br />

significantly with increased ionic strength (up to 0.1 M<br />

nanO 3 ). The experimental data follow (with good agreement)<br />

the Freundlich isotherm.<br />

Acknowledgement (This work has been supported by<br />

Slovak Research and Development Agency project No APVT-<br />

51-017104 and Scientific Grant Agency VEGA, project no.<br />

2/0087/08)<br />

REFEREnCES<br />

1. Smedley P. L., Kinniburgh D. G.: Appl. Geochem. 17,<br />

517 (2002).<br />

<strong>2.</strong> Vaclavikova M., Gallios G. P., Hredzak S., Jakabsky S.:<br />

Clean. Techn. Environ. Policy. 10, 89 (2007).<br />

3. Deliyanni, E. A., Peleka, E. n., Gallios, G. P., Matis, K.<br />

A.: Int J Envir & Waste Manag, (in press).<br />

4. Štefušová K., Václavíková M., Gallios G. P., Jakabský<br />

Š., Kozáková I., Ivaničová L., Gešperová D.: Proceedings<br />

of the 11th International Conference on Environment<br />

and Mineral Processing, Ostrava, 31 May –2 June<br />

2007, (Fečko P., Čablík V., ed.), Part II, p. 71 (Lecture).<br />

5. Aksu Z., Gönen F.: Process Biochem 39, 599 (2004).<br />

6. Deliyanni, E. A., Bakoyannakis, D. n., Zouboulis, A. I.,<br />

Matis, K. A.: Chemosphere 50, 155 (2003).

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