Optimization of Production and Extraction Parameters of Bacillus megaterium
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Optimization of Production and Extraction Parameters of Bacillus megaterium
Journal of Applied Sciences Research, 4(10): 1199-1204, 2008 © 2008, INSInet Publication Optimization of Production and Extraction Parameters of Bacillus megaterium Levansucrase Using Solid-state Fermentation Samia A. Ahmed Department of Chemistry of Natural and Microbial Products National Research Center, Cairo, Dokki, Egypt. Abstract: The use of waste as a raw material is important for government and natural balance. The purpose of this work was to study the production of levansucrase by Bacillus megaterium in solid state fermentation (SSF) using different agricultural residues (orange peels, lemon waste, sawdust, banana waste and wheat bran) as substrates. Maximum enzyme production (140.54 U/g dry solid substrate) was obtained on moistened 5 g sawdust with 55 ml production media (initial pH 6.0) after 72 h incubation at 30 î C under static condition. The extraction of enzyme was found to depend on different parameters like nature of extractant, soaking time, temperature, etc. Among various organic, inorganic solvents and salt solutions tested, maximum extraction was achieved when 10 ml/ g biomass distilled water was adding. The optimum conditions of extraction were 90 min soaking time at 40 î C under agitated condition (160 rpm). Key words: Bacillus megaterium, levansucrase, sawdust, solid state fermentation INTRODUCTION Bacterial levansucrase (EC2.4.1.10) is an extracellular protein found in gram-negative and grampositive bacteria. This protein catalyzes the synthesis of levan (B-2, 6-linked fructan) from sucrose [1 ,2 ]. Levan has potential application in the fields of food as low-caloric sweetener, cosmetic, pharmaceuticals, as antitumor agent based on its physical properties [3 ] and hypocholesterolemic agent[4 ] and increase bifidobacteria population in the intestinal track [5 ]. In the last decades, there are an increasing number of reports about utilization of solid state fermentation (SSF) for production of value added products such as secondary metabolites, organic acid, fuel and enzymes, etc.[6 ]. SSF can be defined as the growth of microorganism on wet solid materials in the absence or near absence of free water and secrete the necessary enzyme for degradation of the available substrate molecules in order to meet their nutritional requirement[7 ]. SSF has gained renewed attention from industry because it becomes a more alternative to submerged fermentation with simpler cultivation equipments, lower capital in v e stm e n t, h ig h e r p ro d u ctiv ity, lo w e ne rgy requirement, less water output, better product recovery, lack of foam build up and reduced bacterial contamination [6 ,8 ]. SSF appears as an interesting lowcost alternative for the production of biomoleculs because agro-industrial residues can be employed as culture media which reduce production costs [9 ]. [8 ]used bran for alpha-amylase production, [ 2 ] produced fructosyltransferase using agricultural by-products.[1 0 ] using wheat bran for producing milk-clotting enzyme, [1 1 ] used melon wastes for lipase production and [1 2 ] used orange bagasse for pectinase production. On the other hand, the application of using agro-industrial waste for SSF solves the pollution problems. Productivity was affected by the nature of solid substrate (SS), SS concentration, level of moisture content, pH of medium, incubation temperature and incubation period. In SSF the products are formed at or near the surfaces of the SS with low moisture content, so it is necessary to select suitable solvents or solution for leaching out the product from the bulky solid mass [8 ]. A common extractant is distilled or deionized water, other extractants have also been used for extract other enzymes such as using sodium chloride solution for protease extraction [1 3 ]. [1 4 ]extracted pectinases from wheat bran by acetate buffer (pH 4.4). This paper reports the optimization of fermentation parameters for levansucrase production by Bacillus megaterium through SSF. Studies on the extraction of levansucrase from sawdust include the effect of some factors which influence the efficiency of leaching out of the enzyme and its efficacy in the leaching technique. M ATERIALS AND M ETHODS M icroorganism: T he bacterial strain Ba cillus megaterium was obtained from the Culture Collection Corresponding Author: Samia A. Ahmed, Department of Chemistry of Natural and Microbial Products National Research Center, Cairo, Dokki, Egypt. Telephone: 002 02 6856074 Fax : +33 4 91 82 85 70 E-mail: [email protected] 1199 J. Appl. Sci. Res., 4(10): 1199-1204, 2008 of the National Research Centre, Dokki, Cairo, Egypt. M aintenance Culture M edium: B. megaterium was maintained on nutrient agar medium, pH 7.0 at 4 î C and was transferred to new slant every week. The following medium was used for production (g/l distilled water): sucrose 80.0; MgSO 4 .7H 2 O 0.3; (NH4) 2 SO 4 2.0; yeast extract 2.0; peptone 2.0 and K 2 HPO 4 2.0. The pH was adjusted to 7.0 before autoclaving. Production Process: To optimize the production process different experiments were carried out. Five grams of different solid substrates (orange peels, lemon waste, banana waste and wheat bran) and 3.0 gm in case of sawdust moistened with 25 ml of production media (pH 7.0) in 250 ml Erlenmeyer flask and incubated at 30 î C for 1 h and 160 rpm. Then the flasks autoclaved for 15 min at 121 î C and each flask inoculated with 2 ml inoculum from 24 h old culture and incubated at 30 î C for 48 h at static condition. The Effect of solid substrate concentration on the enzyme production was measured at different concentrations of sawdust (1, 2, 3, 4, 5, 6 and 7 g). The effect of culture conditions in the present study was carried out at different incubation periods (12, 24, 48, 72 and 96 h), effect of ratio between sawdust and water (1:2, 1:5, 1:8, 1:11 and1:14 w/v) and initial pH (5.0, 6.0, 7.0, 8.0 and 9.0). Extraction Process: The extraction was conducted in 50 ml conical flask containing one gram of fermented biomass and 5 ml of solvent solution and kept for 1 h on a rotary shaker at 160 rpm and 30 î C. The crude extract was centrifuged at 10000xg for 20 min at 4 î C and the clear supernatant obtained was used in the enzyme assays. To optimize the extraction process different experiments were carried out. Effect of Different Solvents: The extraction of the enzyme from the fermented biomass was carried out with distilled water, tap water, and inorganic salt solutions (potassium chloride, magnesium chloride, calcium chloride, and sodium chloride) at different concentrations (0.025, 0.05, 0.075, 0.1 and 0.125 %) and organic solvents (glycerol, methanol, ethanol and acetone) at concentration of 5 %. Effect of Distilled W ater Volume: The investigation was carried out to see the effect of solvent level (1, 5, 10, 15, 20 and 25 ml/g fermented biomass). Effect of Soaking Temperature: To study the effect of temperature on the extraction process the temperature was varied from 20 î C to 60 î C each at 10 î C intervals. Effect of Physical State: Two different extraction conditions were studied stationary and agitation (160 rpm). Effect of Soaking Time: Extraction time was tested (30, 60, 90, 120, 150 and 180 min) keeping all other conditions at optimum levels. Enzyme Assay: Levansucrase assay was performed according to the method of [7 ]. 0.5ml culture filtrate was incubated with 1 ml sucrose solution (20 %) and 0.5 ml acetate buffer (0.1 M , pH 5.2) and incubated at 30 î C for 15 min. The concentration of glucose released by the sucrose hydrolysis activity of levansucrase was measured by the glucose oxidase method with a GODPAP Kit (Sigma). One unit of enzyme activity was defined as the amount of enzyme that produced 1µmol glucose per min. All values given are averages of three determinations. Paper Chromatography: The polysaccharide produced (levan) was precipitated with 2 volumes ethanol and indicated after acid hydrolysis (with 0.1 N HCl in a boiling water bath for 1 h) by paper chromatography. The descending technique was adopted using W hatman No.1 paper and the solvent mixture n-butanol: acetone: water (4: 5: 1). The chromatograms were sprayed with aniline phthalate. RESULTS AND DISCUSSION Due to potential usefulness of levan (produced by levansucrase enzyme) the development of methods for cheaper production of enzyme is very important. One alternative low cost production method is SSF [5 ]. There are several factors, which affect SSF processes and the nature of SS is the most important factor. This not only supplies the nutrient to the culture but also serves as an anchorage for the microbial cells[1 5 ]. The selection of a substrate for SSF depends upon several factors mainly related with cost, availability, consistency, stability, ease of handling and of course the effect on the productivity process. An ideal SS provides all necessary nutrients to the microorganism. However, some of the nutrients may be not present in the SS, so it would be necessary to supplement them externally [5 ]. Several substrates including agricultural crop residues or industrial waste have been used by various workers for SSF. Sawdust is a cheap SS and very little workers used it in SSF. From the various SS used in the present study, sawdust proved to be most suitable for the colonization of B. megaterium, as indicated by the maximum visible growth on the surface of substrate and highest enzyme yield (Fig.1) which is possibly due to its most suitable particle size and consistency required for anchorage. However, it is interesting to know that sawdust is a cheap SS and very little workers used it. [2 ] studied the production of levansucrase by A. oryzae employing a great variety of 1200 J. Appl. Sci. Res., 4(10): 1199-1204, 2008 Fig. 4: Effect of moisture content on levansucrase production. Fig. 1: Effect of different solid levansucrase production. Fig. 2: Effect of sawdust production. level substrate on on levansucrase Fig. 3: Effect of incubation period on levansucrase production. agricultural by-products. They found that, the best results were obtained when rice bran, wheat bran, spent coffee and spent tea used supplemented with yeast extract and complete synthetic media. The effect of sawdust concentration on enzyme production is shown in figure 2. It was observed that 5 g sawdust in the fermentation medium yielded maximum enzyme activity (71.62 U/g dry solid substrate). A further increase in substrate did not increase the enzyme yield significantly because 2 ml inoculume was added to each flask and increase in sawdust level only could not effect the growth of organism [1 6 ]. Fermentation time had a profound effect on enzyme production. Figure (3) showed that the maximum activity (88.57 U/g dry SS) obtained after 72 h of SSF at pH 7.0 and 30 î C. Enzyme level declined with prolonged incubation, this could be due to loss of moisture or denaturation of the enzyme resulting from variation in pH during fermentation. This result is on line with [1 7 ] when obtained the highest level of levansucrase after 72 h. On the other hand, [2 ] found that maximum production of levansucrase by A. oryzae in SSF was 8 h. Moisture content of the substrate is one of the critical factors influencing the outcome of SSF, and is governed by the water-holding-capacity of the substrate, the type of end-product, and the requirement of the microorganism. The inter particle mass transfer within the solid phase to the growing microorganism depends on the substrate characteristics and the moisture content. The results (Fig. 4) pointed to a marked improvement (97.91 U/g dry SS) was achieved by optimizing moisture content. Lower moisture content cause a reduction in solubility of nutrients provided to organism by SS, a lower degree of swelling and higher water tension [5 ]. On the other side, reduction in enzyme 1201 J. Appl. Sci. Res., 4(10): 1199-1204, 2008 Fig. 5: Effect of solvents type on levansucrase extraction from SSF. Fig. 6: Effect of inorganic salt solutions on levansucrase extraction from SSF. Fig. 7: Effect of distilled water volum e on levansucrase extraction from SSF. production at high moisture content may be due to the reduction in substrate porosity, changes in the structure of substrate particles, reduction of gas volume and decreasing in bacterial growth [1 8 ] . pH is among most important factors for any fermentation process and depended upon microorganism because each microorganism possesses a pH range for its growth and activity with an optimum value in between the range [5 ]. The optimal levansucrase production was attained at an initial pH of 6.0 (data not shown). Increasing or decreasing in pH on either side of the optimum value resulted in poor m ic r o b ia l a n d d e c r e a s e in gro w th p ro d u c t fermentation [1 6 ]. SSF is fermentation in the absence of free liquid, and recovery of the fermentation product requires its extraction from the solid fermented medium. The extraction efficiency is critical to the recovery of enzyme from the fermented biomass, hence selection of a suitable solvent is necessary. Organic and inorganic solvents beside tap and distilled water were used in this study. From the results (Fig. 5) it is clear that among all the solvents, distilled water gave the best extraction of levansucrase from the fermented solids. This might be due to dissolution of the all media broth by distilled water which then becomes salt solution and hence able to extract enzyme protein from fermented biomass. Distilled water is a common extractant (available, save and low cost) used by other workers,[1 9 ] used distilled water for extraction of alkaline protease from solid wheat bran fermentation. [2 0 ] extracted xylanase and CMCase enzymes from different solid substrates with distilled water. However, among all salt solutions tested (Fig. 6), sodium chloride 1202 J. Appl. Sci. Res., 4(10): 1199-1204, 2008 Fig. 8: Effect of tem p erature extraction from SSF. on levansucrase less. This may be due to the inhibitory effect of temperature on enzyme activity and make it less stable. Agitation of the fermented biomass with distilled water at 40 î C and 160 rpm gave appreciable amount of levansucrase enzyme compared with stationary condition (data not shown). Agitation was effective for the leaching process due to reduce enzyme adhesion to cell biomass and also disperses the fermented sawdust uniformly in the continuous phase of the solvent [8 ]. Extraction of other enzymes from fermented biomass by agitation process [8 ,1 0 ]. Soaking time was optimized for maximum enzyme recovery from the fermented sawdust. The time period was varied from 30 min to 180 min as shown in figure 9. It was found that 90 min soaking was optimum and beyond that it did not have any additional effect on enzyme extraction indicating that 90 min is the minimum time for total penetration of distilled water through the fermented biomass. Periods of 30 or 60 min seem not be enough for total solubilization of levansucrase enzyme present in sawdust medium.[1 4 ] investigated the effect of incubation time on protease extraction in SSF and found that 30 min provided the best time. On the other side, [8 ] found that 150 min was optimum for extraction of á-amylase from fermented bran. REFERENCES 1. Fig. 9: Effect of soaking time extraction from SSF. on levansucrase (0.05 %) gave the best extraction of enzyme from fermented solid. Increasing extraction up to 0.05 % probably due to the salting-in effect of electrostatic effect of salt[1 0 ]. This result is on line with that obtained by [4 ] who extracted proteolytic enzyme from fermented biomass by elution with sodium chloride. In SSF system free flowing solvent is very much limited. Thus adequate amount of distilled water is required to leach out the enzyme present. The results (Fig. 7) showed that highest levansucrase extraction reaches at ratio 10 ml distilled water: one gram fermented biomass. According to [2 1 ] the amount of solute increase with the increase of solvent volume. Decreasing in enzyme extraction when lower volume of solvent was used might be due to insufficient solvent volume to penetrate the solid fermented mass [8 ]. Excessively large volume of extractant used for greater extraction would also yield too dilute enzyme solutions to be profitably utilized. Maximum yield of enzyme was obtained at 40 î C (Fig. 8), but at the higher temperature the yield was 2. 3. 4. 5. 6. 1203 Ben-Ammar, Y., T. Matsubara, K. Ito, M. Iizuka and N. M inamiura, 2002. Some properties of levansucrase of Bacillus natto stabilized with periodate oxidatized yeast glucomannan. Enz. Microb. Technol., 30: 875-882. 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