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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 />

at 25 °C by the agitating at the speed of 150 rpm. The cells<br />

were harvested from the growth medium by membrane filtration<br />

(pore size 0.85 µm). Bacteria suspension was prepared<br />

with concentration of bacteria 1.2 × 10 9 ml –1 in accordance to<br />

MacFarland standards.<br />

P r e p a r a t i o n o f C o p p e r M o d e l<br />

S o l u t i o n s<br />

The model solution of Cu (II) was prepared by dissolving<br />

of CuSO 4 . 5H2 O in deionized water in various concentrations<br />

ranging from 0.01; 0.02; 0.04; 0.06; 0.1; 0.5; 1; 1.5; 2; <strong>2.</strong>5;<br />

3 to 5 mM. Previous studies showed that at pH 5 is the most<br />

effective copper sorption. The initial pH of the solutions was<br />

adjusted to 5 by adding 0.1M HnO 3 or 0.1M naOH for the<br />

biosorption experiments. Various Cu(II) concentrations and<br />

concentration after sorption process were measured by atomic<br />

absorption spectrofotometer (Varian AA240 Z, AA240<br />

FS, Australia).<br />

C o l u m n S t u d i e s<br />

In this study glass columns were used for experiments.<br />

The filtration column was 130 mm high with an inner diameter<br />

of 40 mm. Column was packed with appropriate amounts<br />

of each sorbent in layers (100 g of quartz sand, 0.5 g of bentonite<br />

and 0.1 g of synthetic magnetite). 50 ml of bacteria suspension<br />

was passed through the column to adjusted the adhesion<br />

of bacteria cells. Two types of filtration columns were<br />

prepared. In both types there was 45 mm depth of ceramic<br />

medium, one reached with bacteria (biotic filter) and another<br />

filter without bacteria medium (abiotic filter). Then 50 ml of<br />

Cu(II) model solution was passed through the column at a<br />

constant flow rate of 1.5 ml min –1 .<br />

Fig. 3. Sorption columns<br />

Results<br />

Bioceramic filters composed of quartz sand + bentonite<br />

+ synthetic magnetite + bacteria were used for the sorption<br />

of copper. These two types of filters were compared in<br />

sorption efficiency. The effect of initial concentration on the<br />

percentage removal of copper by biotic and abiotic filters is<br />

s500<br />

shown in Fig. <strong>2.</strong> Fig. <strong>2.</strong> demonstrates that sorption was more<br />

effective in case of biotic filters. The work was carried out at<br />

the pH (5) of model solution because this pH value is for copper<br />

sorption optimum. The maximum removal of Cu(II) was<br />

attained at a concentration 63.5 mg dm –3 Cu. High removal<br />

efficiency (> 95 %) was obtained over the copper (II) concentration<br />

range 1–100 mg dm –3 . However the removal percentage<br />

decreased with increasing the copper (II) concentration<br />

( > 100 mg dm –3 ). Therefore this method seems to be suitable<br />

for the removal of relatively lower concentration of copper.<br />

Fig. <strong>2.</strong> Effect of initial copper concentration on percent removal<br />

of copper by biotic and abiotic filter<br />

Conclusions<br />

The present study showed that the bioceramic filters<br />

based on quartz sand, bentonite, synthetic magnetite and bacteria<br />

can be used as an effective adsorbent of copper. The<br />

results of experiments showed high removal of copper by<br />

both types of model filters at concentrations ranging from<br />

0.01 to 1.5 mM Cu(II). At higher concentrations removal<br />

of copper decreased. The percentage removal was more effective<br />

in biotic filters with baceria medium; however the<br />

difference compared with abiotic filter was not so marked.<br />

Therefore in further experiments bacteria medium with higher<br />

concentration of bacteria cells is needed. In the further<br />

study various iron oxides (hematite, goethit) and clay minerals<br />

(zeolite, kaolinite) will be used in experiments and their<br />

sorption efficiency will be compare.<br />

This work has been supported by the Slovak Academy of<br />

Sciences (VEGA 2/0049/08).<br />

REFEREnCES<br />

1. Cassela R. J.: Microchem. J. 72, 17 (2002).<br />

<strong>2.</strong> Meena A. K., Mishra G. K., Rai P. K., Rajagopal Ch.,<br />

nagar I.: J. Hazard. Mater. B122, 161 (2005).<br />

3. Kooner Z. S.: Environ. Geol. 21, 242 (1993).<br />

4. Wu. G., Li L. Y.: J. Contam. Hydrol. 33, 313 (1998).

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