Indian Journal of Biotechnology Vol 12, July 2013, pp 429-431 Comparative studies for chitosan yield and chelating ability of Aspergillus niger and Rhizopus oryzae S Bhuvaneshwari and V Sivasubramanian* Department of Chemical Engineering, National Institute of Technology, Calicut 673 601, India Received 21 February 2012; revised 17 April 2012; accepted 10 June 2012 Chitosan is a natural polysaccharide comprising copolymer of glucosamine and N-acetyl glucosamine, and can be obtained by the deacetylation of chitin. Due to its biodegradability, biocompatibility and low toxicity, chitosan has received increased attention as one of the promising renewable polymeric materials for its various applications in the bioremediation, pharmaceutical, chemical and biomedical industries. In the present study, chitosan was extracted from cell walls of Aspergillus niger and Rhizopus oryzae, and characterized for mol wt, viscosity and degree of deacetylation. Further, effect of metal concentration, pH and contact time on the adsorption of heavy metals from aqueous solutions by extracted-chitosan was studied. The sorption properties were also compared using live biomass and the chitosan from A. niger and R. oryzae. It has been found that A. niger gave good yield and the extracted chitosan also had high sorption capacity compared to the chitosan derived from R. oryzae. The maximum adsorption capacity for copper (79.65%) and chromium (87.61%) was obtained using A. niger at optimized conditions. Fourier transform infrared (FT-IR) analysis indicated that hydroxyl and amine groups of chitosan structure were involved in the mechanism of copper and chromium adsorption. Keywords: Aspergillus niger, chitosan, chromium, copper, Rhizopus oryzae It has been well known that many biological materials accumulate metals. There is an increasing interest in investigating such biological adsorbents for a variety of applications as the conventional methods have disadvantages like incomplete removal, high energy and reagent requirements1. Chitosan is a natural polysaccharide comprising copolymer of glucosamine and N-acetyl glucosamine. It is commercially produced from shrimp and crab shell chitin via its deacetylation by strong alkalis at high temperature for long periods of time2. When chitosan is dissolved in _______________ *Author for correspondence: Tel: +91-495-2285406; Fax: +91-495-2287250 Mobile: +91-9446547421 E-mail: [email protected] an acid solution, it becomes a cationic polymer due to the protonation of free amino groups on the C-2 position of pyranose ring. The cationic properties in acidic solution give it the ability to interact readily with negatively charged molecules, such as, fats, cholesterols, metal ions and proteins3. The chitosan derived from different sources are heterogeneous with respect to physiochemical properties4. Chitin containing microbial biomass and in particular fungal biomass is well suited for chitosan synthesis. Such biomass usually has 10 to 20% chitin based on dry wt of the biomass. In order to prepare the high quality chitosan, it is desirable that the microbial biomass be produced in a substantially controlled manner, having relatively uniform temperature and nutrient levels during the growth of the biomass. Fungi, in addition, can be grown easily on any simple medium or industrial byproducts, and this will also free the environment from pollution concerns5. Moreover, in order to sustain the marine biodiversity, it is also advisable to use microorganism for the chitosan production. In the present investigation, efforts were made to extract chitosan from the Aspergillus niger and Rhizopus oryzae for the adsorption of heavy metals. All the chemicals used were of analytical grade and samples were prepared using double distilled water. The freeze dried cultures of A. niger (strain no. 281) and R. oryzae (strain no. 553) were collected from Microbial Type Culture Collection (MTCC), Institute of Microbial Technology, Chandigarh, India. Subsequently, A. niger and R. oryzae were sub-cultured in PDB (potato dextrose broth) and Czapek medium for 3 and 4 d, respectively, and then both were transferred on PDA (potato dextrose agar) plates at room temperature and pH 7. PDA plates were then kept under same conditions for about 4 d or until the plates were fully grown. The grown fungus (microbial biomass) was mass cultivated6. About 250 mL of sodium hydroxide solution (4% w/v) was mixed with 250 g of microbial biomass of A. niger and R. oryzae. A strong exothermic reaction occurred when fungal biomass was dissolved into sodium hydroxide solution. The flask containing the biomass in the sodium hydroxide solution was placed in a pre-heated oven at about 120°C for 30 min. After INDIAN J BIOTECHNOL, JULY 2013 430 heating, the warm solution was filtered. The residuals were completely washed with deionized water. This pretreated biomass containing chitosan-glucan complex was rinsed with water many times until the pH of filtered solution reached to less than pH 9. After rinsing, the solids were transferred to a beaker and glacial acetic acid was added till pH 3.5 was obtained. The mixture was stirred for about 10 min to extract chitosan from the glucan and then the mixture was centrifuged to6,7. The crude chitosan was washed several times with distilled water and air dried at 20°C to a constant wt. Biosorption studies for the recovery of copper and chromium was carried out using potassium chromate and copper sulphate solutions in distilled water. Known amount of chitosan was introduced to metal solution at different metal concentration and pH. Intimate contact for biomass and metal solution was provided by agitating it at low speed of 150 rpm in a rotary shaker. At different contact time, the biomass was separated by filtering and the filtrate was analyzed using Chemito Atomic absorption spectrophotometer (AA 203). The chitosan content of fungi depends on fungal strains, mycelium age, cultivation medium and cultural conditions8. The extracted chitosan from fungal cell walls of A. niger and R. oryzae was analysed by FT-IR spectrophotometer (Thermo Nicolet Model-Avater 320 model) and compared with the spectrum of standard chitosan derived from crab shell5,9. The peaks obtained from the two samples were found similar to the peaks of standard chitosan (Figs 1a-c). This clearly reveals that the extracted fraction from the cell walls of A. niger and R. oryzae was chitosan. The yield of fungal biomass and chitosan as well as degree of deacetylation (DD), viscosity and mol wt of chitosan from the both fungi were determined10 and results are presented in Table 1. The results clearly show that the amount of biomass produced and the yield of extracted chitosan was higher in case of A. niger in comparison to R. oryzae. Moreover, the chitosan extracted from A. niger had higher DD, viscosity and mol wt as compared to chitosan from R. oryzae. Biosorption of Cu and Cr ions by chitsan from A. niger and R. oryzae showed only slight increase with the increase in initial metal concentration from Table 1—Physio-chemical characteristics of fungal chitosan Chitosan source Biomass Chitosan Mol wt Degree of Viscosity obtained produced (kDa) deacetylation (cp) (g/L) (mg/g) (%) A. niger 266.7 724.9 331.436 85.90 5.49 R. oryzae 98.3 121.3 85.142 82.12 2.98 Fig. 1 (a-c) FTIR spectrum: a. Standard chitosan derived from crab shell chitin; b. Chitosan derived from R. oryzae; & c. Chitosan derived from A. niger SHORT COMMUNICATIONS Table 2—Effect of contact time on biosorption of metals by fungal chitosan Biosorption (%) A. niger Forms Chitosan Live biomass rd th Metals 3 d 5 d Cu 73.87 79.65 Cr 76.48 87.61 Cu Cr 55.1 68.22 67.76 70.87 R. oryzae th rd 7 d 80.11 88.02 3 d 5th d 7th d 77.88 77.95 78.16 67.64 74.76 74.27 68.26 71.09 61.19 66.09 66.18 63.66 66.09 66.10 431 5th d for both chitosan and fungal biomass (Table 2). However, no substantial increase in metal sorption was observed beyond 5th d. Therefore, 5 d contact time for biosorption was optimum for recovery of Cr and Cu for both chitosan and fungal biomass. Moreover, in case of both chitosan and live fungal biomass, pH 5 was observed optimal for biosorption of both the metal ions (Fig. 2). Overall, copper and chromium recovery was recorded higher in A. niger compared to R. oryzae. Thus, biosorption using chitosan is a promising technology for metal sorption because of its cost effectiveness and high efficiency. Acknowledgement The study was financially (Project No.: SR/FTP/CS-68/2007) supported by the Department of Science and Technology, Government of India, New Delhi. References Fig. 2Effect of pH on % metal recovery by chitosan derived from A. niger and R. orzyae, and their live biomass. 2 to 6 mM, whereas no increase in biosorption was observed beyond 6 mM initial concentration (original data not shown). Therefore, 6 mM was considered as an optimal metal concentration for further studies. Moreover, biosorption of Cu and Cr ions did not show much variation between the chitosan of both the fungi at all the initial concentrations (2 to 10 mM) used. Further studies were conducted to assess the biosorption capacity of chitosan from both A. niger and R. oryzae and their live biomass at various contact time and pH. The results show that chitosan from both the fungi had a higher biosorption capacity as compared to their live fungal biomass for both the metals at different contact time and pH (Table 2; Fig. 2). The difference was due to chitosan cationicity in acidic solution because of the presence of large number of amino groups, which were reactive for metal cations11. In case of both A. niger and R. oryzae, increase in contact time increased the biosorption of Cu and Cr ions only up to 1 Alluri H K, Ronda S R, Settalluri V S, Bondili J S, Suryanarayana V et al, Biosorption: An eco-friendly alternative for heavy metal removal, Afr J Biotechnol, 6 (2007) 2924-2931. 2 Eom T K & Lee K M, Characteristics of chitosanases from Aspergillus fumigates KB-1, Arch Pharm Res, 26 (2003) 1036-1041. 3 Nomanbhay S M & Palanisamy K, Removal of heavy metal from industrial wastewater using chitosan coated oil palm shell charcoal, Electron J Biotechnol, 8 (2005) 43-53. 4 Nadarajah K, Kader J, Mazmira M & Paul D C, Production of chitosan by fungi, Pak J Biol Sci, 4 (2001) 263-265. 5 Limam Z, Selmi S, Sadok S & El Abed A, Extraction and characterization of chitin and chitosan from crustacean by-products: Biological and physicochemical properties, Afr J Biotechnol, 10 (2011) 640-647. 6 Franco L de O, Maia R de C C G, Porto A L F, Messias A S, Fukushima K et al, Heavy metal biosorption by chitin and chitosan isolated from Cunninghamella elegans (IFM 46109), Braz J Microbiol, 35 (2004) 243-247. 7 Cabuk A, Ilhan S, Filik C & Caliskan F, Pb2+ biosorption by pretreated fungal biomass, Turk J Biol, 29 (2005) 23-28. 8 Thangaraj M & Lipton A P, Species-specific proteins in closely-related seahorses, Curr Sci, 86 (2004) 1645-1647. 9 Suksabye P, Thiravetyan P, Nakbanpote W & Chayabutra S, Chromium removal from electroplating wastewater by coir pith, J Hazard Mater, 141 (2007) 637-644. 10 Kasaai M R, Arul J & Charlet G, Intrinsic viscositymolecular weight relationship for chitosan, J Polym Sci (B) Polum Phys, 38 (2000) 2591-2598. 11 Eric Guibal, Interactions of metal ions with chitosan-based sorbents: A review, Sep Purif Technol, 34 (2004) 155-161.
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