The biosorption of cadmium and arsenic from aqueous solutions onto the unmodified compact biomass of microscopic filamentous fungus Aspergillus clavatus DESM. was studied in the concentrationrange of 0.25 – 100 mg.l-1. The experimental biosorption results for arsenic and cadmium followed well the Freundlich equilibrium sorption model

Cernansky, S

Hiller, E

Littera, P

Urík, M

Ševc, J

English

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African Journal of Biotechnology Vol. 6 (16), pp. 1932-1934, 20 August 2007 Available online at http://www.academicjournals.org/AJB ISSN 1684–5315 © 2007 Academic Journals     Short Communication  Biosorption of arsenic and cadmium from aqueous solutions  Slavomír eranský1*, Martin Urík2, Jaroslav Ševc2, Pavol Littera1 and Edgar Hiller3  1Comenius University in Bratislava, Faculty of Natural Sciences, Department of Ecosozology and Physitactics, Mlynská dolina, 84215 Bratislava, Slovak Republic. 2Comenius University in Bratislava, Faculty of Natural Sciences, Geological Institute, Mlynská dolina, 842 15 Bratislava, Slovak Republic. 3Comenius University in Bratislava, Faculty of Natural Sciences, Department of Geochemistry, Mlynská dolina, 842 15 Bratislava, Slovak Republic.  Accepted 2 July, 2007  The biosorption of cadmium and arsenic from aqueous solutions onto the unmodified compact biomass of microscopic filamentous fungus Aspergillus clavatus DESM. was studied in the concen-tration range of 0.25 – 100 mg.l-1. The experimental biosorption results for arsenic and cadmium followed well the Freundlich equilibrium sorption model.  Key words: Biosorption, arsenic, cadmium, microscopic filamentous fungi.   INTRODUCTION  Microscopic filamentous fungi as a part of microbial com-munities influence transformation and distribution of metal (loid)s in the environment. Interactions between microorganisms and ions of different metal (loid)s can be divided in two basic categories; transformations, that lead to the mobilization of heavy metals (bioleaching, biolo-gical methylation and reduction), and transformations that immobilize metal(loid)s, such as biosorption, or different types of microbial precipitation, or binding of metalloids to macromolecules (Gadd, 2000; Slaninka et al., 2006; Šimonoviová and Franková, 2001). Nowadays, environmental biotechnologies use these interactions to decrease concentration of potentially toxic chemicals in wastewaters or industrial substrates. The most frequent biotechnology is biosorption. The biosorp-tion is passive non-metabolic process of binding various chemicals on biomass (Volesky, 1990), including physic-co-chemical interactions, adsorption and ion exchange (Gadd and White, 1993). In case of biosorption, ion exc-hange is the most important mechanism, that is realized by  interaction  between  ions  of  metal  (loid)s and active    *Corresponding author.E-mail: cernanskys@fns.uniba.sk. Tel: +421260296560. groups on cell wall biopolymers. The biomass represents polyelectrolyte with amino, carboxyl, phosphate, phenol and sulphydril active groups (Naja et al., 2005). Biosorption by the biomass of microscopic filamentous fungi represents economically and technically relevant technology for bioremediation of wastewaters contamina-ted with metal (loid)s (Pmpel and Scinner, 1993). In this paper was studied potential of microscopic filamentous fungus Aspergillus clavatus to sorb ions of cadmium and arsenic from aqueous solutions.   MATERIALS AND METHODS  Preparation of biomass  As a sorbent was used biomass of microscopic filamentous fungus A. clavatus DESM. isolated from a locality Pezinok – Kolársky vrch (Slovakia), highly contaminated with metal(loid)s. The biomass used in experiment was prepared by static cultivation. 50 mL of Sabouraud medium (SAB – Himedia, Mumbai, India) were inocu-lated with 5 mL of spore suspension of microscopic filamentous fungus A. clavatus. The biomass was cultivated for two weeks under laboratory conditions. Prepared biomass was 5 to 6 cm in diameter and 0.5 cm in height. The biomass was then isolated from the SAB medium by filtration and centrifugated for 10 min to remove the rest of the medium (3000 rpm; MPW-340, Mechanika Precyzyjna, Poland). The biomass was than dried and subsequently the weight for each sample was adjusted to 1.11 g. Cernansky et al.        1933    Table 1. Amount of immobilized arsenic for aqueous solution by microscopic filamentous fungus Aspergillus clavatus (n = 3).  Amount of cadmium in 50 ml of solution before sorption (mg) Amount of arsenic in 50 ml of solution after sorption (mg) Amount of immobilized arsenic by biomass (mg) Arsenic immobilized by biomass (%) 0.0125 0.0108 0.0017 13.6 0.025 0.0214 0.0036 14.4 0.05 0.0456 0.0044 8.80 0.125 0.1147 0.0103 8.24 0.25 0.2207 0.0293 11.7 0.5 0.4547 0.0453 9.06 1.25 1.1434 0.1066 8.53 2.5 2.3567 0.1433 5.73 5.0 4.5400 0.4600 9.20    Table 2. Amount of immobilized cadmium for aqueous solution by microscopic filamentous fungus Aspergillus clavatus (n = 3).  Amount of cadmium in 50 ml of solution before sorption (mg) Amount of cadmium in 50 ml of solution after sorption (mg) Amount of immobilized cadmium by biomass (mg) Cadmium immobilized by biomass (%) 0.025 0.0137 0.0113 45.2 0.05 0.0253 0.0247 49.4 0.125 0.0838 0.0412 33.0 0.25 0.1986 0.0514 20.6 0.5 0.4544 0.0456 9.12    Biosorption of arsenic and cadmium from aqueous solutions  Aqueous solutions (50 mL) with desired concentration of arsenic (0.25, 0.5, 1, 2.5, 5, 10, 25, 50 or 100 mg.L-1 As) or cadmium (0.5, 1, 2.5, 5 or 10 mg.L-1 Cd) were prepared from stock solutions of pentavalent arsenic oxyanion (AsO4-3) or bivalent cadmium ion (Cd(NO3)2) stabilized in 0.5 M HNO3 (Merck, Germany). All experi-ments were replicated in three runs. The biomass was in direct contact with prepared aqueous solution for one hour. Each system was shaking for 1 h on shaker (120 rpm, Unimax 2010, Heidolph, Germany). After an hour's sorption, compact biomass was mecha-nically isolated from solution and washed with 20 ml of deionized water. Subsequently the total arsenic and cadmium content in aqueous solution was measured as described below (Bujdoš et al., 2000).   Analytical method  The arsenic standard was prepared by a dilution of stock solutions of As 1.000 g.L–1 (Merck, Germany, H3AsO4 in 0.5 mol.L–1 HNO3) and of Cd 1.000 g.L-1 (Merck, Germany, H3AsO4 in 0.5 mol.L–1 HNO3). The total concentration of arsenic in aqueous solution was analyzed by using hydride generation atomic absorption spectro-metry (HG AAS), using the Perkin-Elmer Atomic Absorption Spectrometer model 1100 (USA) equipped with a hydride generator LabTech HG-2 (Czech Republic). Cadmium was analyzed by using flame atomic absorption spectrometry (FAAS), using the Perkin-Elmer Atomic Absorption Spectrometer model 1100 (USA).   RESULTS AND DISCUSSION  In this paper was determined the ability of fungal A. clavatus strain to biosorb (immobilize) oxyanions of arse-nic (0.25 – 100 mg.L-1) and bivalent ion of cadmium (0.5 - 10 mg.L-1 Cd) from aqueous solutions. Amounts of biosorbed arsenic and cadmium onto fungal biomass are shown in Tables 1 and 2. The results has shown that ar-senic oxyanions and cadmium behave differently by the low concentrations of metal (loid)s in aqueous solution. Sorption of arsenic onto unmodified biomass of A. cla-vatus in concentration range from 0.5 to 5 mg.L-1 is low (around 10 % from original amount of arsenic in solution), while the biosorption of cadmium is nearly three times higher. Lower sorption of arsenic by biomass, which is in solution presented as negative charged oxyanion, may relate with repulse electrostatic interactions between negatively charged surface of biomass and AsO43-. Experimental results from biosorption are usually quan-titative evaluated by using adsorption isotherm models, which show dependency of sorbed amount of certain chemical compound in sorbent Seq (concentration of metal (loid) in biomass of microscopic filamentous fun-gus) and concentration of this chemical compound in aqueous solution Ceq (equilibrium concentration of metal (loid) in aqueous solution after biosorption). Quantitative evaluation of biosorption using equilibrium adsorption models is important for constructing and opti-mizing parameters of adsorption system for removal of toxic metal (loid)s from waters. Biosorption of arsenic and cadmium were evaluated in this paper using standard adsorption model, Freundlich isotherm, which expects heterogeneous distribution of energy of adsorption sites on sorbent. Freundlich adsorption isotherm has form: 1934           Afr. J. Biotechnol.    Table 3. Freundlich constants for biosorption of cadmium and arsenic onto biomass of Aspergillus clavatus strain from aqueous solutions.  Metal logKF (mg.g-1)/(mg.ml-1)N N R2 Cadmium Cd2+ -0.685 (-1.09 – -0.282) 0.435 (0.289 – 0.580) 0.762 Arsenic AsO43- 0.413 (0.253 – 0.574) 0.890 (0.826 – 0.955) 0.970      Figure 1. Application of Freundlich model to arsenic and cadmium biosorption onto biomass of fungal Aspergillus clavatus strain.    NeqFeq CKS =                                      (1)  and its linear form is:  eqFeq CNKS logloglog +=            (2)  where Seq is adsorbed amount of metal(loid) onto bio-mass (mg.g-1), Ceq is equlibrium concetration of metal (loid) in aqueous solution (mg.ml-1), KF and N are Freundlich constants.  For determination of Freundlich constants its linear form (2) was used and their values along with determi-nation coefficients for biosorption of arsenic and cadmium are shown in Table 3.  The experimental biosorption results for arsenic and cadmium followed well the Freundlich equilibrium sorp-tion model in the concentration range of 0.25 – 100 mg.l-1 (Figure 1), and dependency of Seq and Ceq were statis-tically significant (P < 0,001 for As and P < 0,05 for Cd). Adsorption isotherm for biosorption of arsenic is relatively linear because Freundlich exponent N is around 1 (Table 3). This shows that there were not all of the active sites occupied in certain concentration range, while the absor-ption capacity of biomass did not change. The ability of biomass to sorb arsenic without respect to initial concen-tration of arsenic in aqueous solution also support relative constant of immobilized arsenic by biomass, which are shown in Table 1. On the other hand, adsorption isotherm of cadmium is significantly nonlinear and has convex form (N < 1), which refers to lower affinity of cadmium to biomass in higher initial concentration of cadmium in aqueous solution. This means that sorption capacity of biomass for cadmium ions is limited in this concentration range (Table 2).   Conclusion  Application of biosorption for removal of potentially toxic metal (loid)s from contaminated waters is a problem that is mostly studied under laboratory conditions. But we can plan real technologies useable for in situ bioremediation only when all of the parameters of this technology are verified mathematically to guarantee economical advent-age of this technology in comparison with conventional chemical methods. This is why laboratory experiments represent important step before the construction of large-scale bioreactor. In this paper the biosorption of cadmium and arsenic from aqueous solutions onto the unmodified compact biomass of microscopic filamentous fungus A. clavatus DESM. was studied in the concentration range of 0.25 – 100 mg.l-1. Mathematical model (Freundlich isotherm) from experimental results suggests potential of biomass of microscopic filamentous fungi for removing of toxic metal (loid)s from contaminated waters.   ACKNOWLEDGEMENTS  This work was supported by grants VEGA 1/3462/06, VEGA 1/4361/07, VEGA 1/2352/05, UK/197/2007, UK /199/2007.   REFERENCES  Bujdoš M, Kubová J, Streško V (2000). Problems of Selenium Fractionation in Soils Rich in Organic Matter. Anal. Chim. Acta 408: 103-109. Gadd GM (2000). Bioremedial potential of microbial mechanisms of metal mobilization and immobilization. Curr. Opin. Biotechnol. 11: 271-279. Gadd GM, White C (1993). Microbial treatment of metal pollution – a working biotechnology? Trends Biotechnol. 11: 353-359. Naja G, Mustin C, Volesky B, Berthelin J (2005). A high-resolution titrator: a new approach to studying binding sites of microbial biosorbents. Water Res. 39: 579-588. Pmpel T, Schinner F (1993). Native fungal pellets as biosorbent for heavy metals. FEMS Microbiol. Rev. 11: 159-164. Šimonoviová A, Franková E (2001). Soil microfungi in toxic and heavy metal environment. Ekologia 20: 242-249. Slaninka I, Jurkovi , Kordík J (2006). Ekologická záaž vodného ekosystému arzénom v oblasti odkaliska Poša (Východné Slovensko). Vodní hospodáství 11: 275-277. Volesky B (1990). Biosorption of heavy metals. CRC Press, Boca Raton, USA. 

Biosorption of arsenic and cadmium from aqueous solutions

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Biosorption of arsenic and cadmium from aqueous solutions

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