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Asian Journal of Biochemistry

Year: 2012 | Volume: 7 | Issue: 3 | Page No.: 123-132
DOI: 10.3923/ajb.2012.123.132
Purification and Characterization of Extracellular Protease from Halotolerant Bacterium Virgibacillus dokdonensis VITP14
V. Devi Rajeswari, G. Jayaraman and T.B. Sridharan

Abstract: In this study extracellular protease was purified with ammonium sulphate precipitation, dialysis, gel filtration and ion exchange chromatography. The purity was checked with MALDI-TOF and SDS-PAGE. Confirmation of protease was done with zymogram. The molecular weight of the protease was found to be 36 kDa. MALDI-TOF analysis of the protein showed the Molecular weight confirmation of the studied protease. Further the enzyme was characterized for its maximal activity with different pH, temperature, salt concentration and inhibitors. The maximal activity was found at pH 7.0, 40°C, 1.5 M salt concentration and found to be serine protease.

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V. Devi Rajeswari, G. Jayaraman and T.B. Sridharan, 2012. Purification and Characterization of Extracellular Protease from Halotolerant Bacterium Virgibacillus dokdonensis VITP14. Asian Journal of Biochemistry, 7: 123-132.

Keywords: characterization, Virgibacillus, Extracellular protease and purification

INTRODUCTION

Haloalkaliphilic bacteria have been mainly focused on its molecular diversity and its phylogeny, in-depth exploration of its enzymatic potential and properties have to be revealed. Till date only few haloalkaliphilic enzymes have been studied and reported about its potential uses (Gupta et al., 2005; Patel et al., 2005; Studdert et al., 1997, 2001; Seitz et al., 1997; Eddy and Jablonski, 2000). Even though there are enzymes used in biotechnological and industrial applications, which will not meet the growing demands. Due to this, researchers have recently focused on isolation and characterization of the enzyme from various microbes. Especially, extremophiles is a valuable source of enzyme for a variety of applications (Herbert et al., 1992; Eichler, 2001; Kathiresan and Manivannan, 2007; Ikram-ul-Haq et al., 2003).

Proteases are important enzymes which dominate two-third of the detergent enzyme market (Niehaus et al., 1999; Gupta and Roy, 2002). I also plays an important role in the hydrolysis of proteins by specific catalytic action (Manivannan and Kathiresan, 2007). Bacillus is the major producer of most commercial proteases (Mehrotra et al., 1999; Abdel-Naby et al., 1998; Mabrouk et al., 1999; Beg and Gupta, 2003; Phadatare et al., 1993; Hoq et al., 2005). Despite the presence of proteases, enzymes with specific properties are the major interest for scientists which led them to find new sources of protease with various specific properties and functions (Joo and Chang, 2005; Bezerra et al., 2005; Mei and Jiang, 2005). One such novel source is marine microbes. Due to its extreme physiological characteristics, metabolic patterns and utilization of nutrient these microbes are expected to possess unique properties. Reports with halophilic proteases are very limited in the literature. The present study showed the purification and characterization of halotolerant protease from a marine bacterium Virgibacillus dokdonensis.

MATERIALS AND METHODS

Micro organism used: Halotolerant bacterium VITP14 was isolated and previously characterized for its 16S rRNA sequencing was used for purification and characterization of its extracellular protease (GenBank accession number HQ829428).

Preparation of inoculums: Production of enzyme was done in Zobell marine broth. A 5% inoculum was added to Zobell broth from an overnight culture (OD 2.1 at 660 nm) and incubated for 48 h at 37°C (100 rpm); the culture was drawn after incubation and centrifuged at 10,000 rpm for 10 min at 4°C. This collected culture supernatant was used for further analysis.

Ammonium sulphate precipitation: The culture filtrate was precipitated with the addition of ammonium sulphate. The salt was slowly added to the filtrate to obtain 75% saturation with gentle stirring and kept at 4°C for complete precipitation to occur. The precipitate was collected by centrifugation at 10,000 rpm for 15 min at 4°C. The collected precipitate was dissolved in minimum quantity of 1 mM tris-HCl buffer (pH 8.0). This precipitate was lyophilized and further purified in ion exchange and gel filtration chromatography (Padmakar et al., 2005).

Ion exchange chromatography: The precipitated enzyme solution was loaded at a flow rate of 0.2 mL min-1 to (2x7 cm), pre-equilibrated with 1 mM Tris-HCl buffer of pH 8.0 and the eluted fractions (1 mL each) were collected. After loading the sample, column was washed with the same buffer until the reading of the eluted buffer at 280 nm was zero. The bound proteins were then eluted with a concentration gradient of sodium chloride (0-0.5 M NaCl) in the same buffer and fractions of 2 mL each were collected at a flow rate of 0.2 mL min-1. Protein concentration of each fraction was determined by measuring the absorbance at nm and each fractions were assayed for protease activity. Fractions with high specific activity were pooled and then concentrated by lyophilization (Singh et al., 2001).

Gel filtration chromatography: One milliliter of partially purified, lyophilized enzyme was loaded to a Sephadex-G-75 (Fluka Chemicals, Buchs, Switzerland) column (1.25x35 cm) pre-equilibrated with 1 mM of Tris-HCl buffer (pH 8.0) and then eluted with the same buffer. Fractions of 2 mL each were collected at a flow rate of 2.5 mL h-1. Protein concentration of each fraction was determined by measuring absorbance at 280 nm and all the collected fractions were assayed for protease activity. The active fractions were pooled, concentrated by lyophilization and purity was checked in SDS-PAGE (Sana et al., 2006).

Enzyme assay: The proteolytic activity was assayed by the modified method of Kunitz using casein as the substrate. The reaction was carried out in a tube containing 500 μL of 2% (w/v) casein in 1 mM Tris-HCl buffer (pH 8.0) with enzyme from the fractions, incubated at 37°C for 10 min. The reaction was terminated by adding 2.5 mL of 10% (w/v) trichloroacetic acid (TCA), kept at room temperature for 30 min and then centrifuged at 10,000 xg for 8 min. The absorbance was measured against a blank at 280 nm. One unit of protease activity was defined as the amount of enzyme required to liberate 1 μmol of tyrosine in 1 min under standard assay conditions. The specific activity is expressed in units of enzyme activity/mg of protein (Ibrahim and Ali-salamah, 2009).

Polyacrylamide gel electrophoresis: The purity and molecular weight of the enzyme was determined in SDS-PAGE using a 5% (w/v) stacking and a 12% (w/v) separating gels. Samples were prepared by mixing purified enzymes in a ratio of 1:1 (v/v) with sample buffer. Before loading the samples, it was heated at 100°C for 5 min. After the run the gels were stained with 0.25% coomassie brilliant blue R-250 in 45% ethanol-10% acetic acid and destained with 5% ethanol with 7.5% acetic acid. The molecular weight of the enzyme was identified by compared with the commercial standard protein marker (Banik and Prakash, 2006).

Detection of proteolytic activity on polyacrylamide gels-protease zymogram: Zymography was performed in conjunction with PAGE according to the method described by Garcia-Carreno et al. (1993) with slight modification. The sample was not heated before electrophoresis. After electrophoresis, the gel was submerged in 100 mM glycine-NaOH buffer (pH 10.0) containing 2.5% Triton X-100 for 30 min, with constant agitation to remove SDS. Triton X-100 was then removed by washing the gel three times with 100 mM glycine-NaOH buffer (pH 10.0). The gel was then incubated with 1% (w/v) casein in 100 mM glycine-NaOH buffer (pH 10.0) for 20 min at 50°C. Finally, the gel was stained with Coomassie Brilliant Blue R-250. The development of clear zones on the blue background of the gel indicated the presence of protease activity.

MALDI-TOF mass spectrometry analysis: Molecular mass was analyzed in MALDI-TOF mass spectrometry using a Voyager-DE PRO MALDI-TOF mass spectrometer (Applied Biosystems, Foster City, CA, USA). One microliter of sample in TFA 0.1% was mixed with 2 mL of the matrix prepared with α-cyano-4-hidroxy-cinnamic acid (Sigma), 60% acetonitrile and 0.1% v/v TFA. The mass of the protein was analyzed in linear analysis mode using an acceleration voltage of 25 kV, with the laser fixed in 2890 mJ com2 and a delay of 300 ns.

Effect of pH: To determine the effect of pH, the purified enzyme was incubated at different pH range (6.0 to 9.0). To 500 μL buffer of different pH range, 500 μL of purified enzyme was incubated at 37°C for 30 min. After incubation, casein was added to the reaction and incubated for 10 min and the reaction was stopped by the addition of TCA and measured the absorbance at 280 nm (Anvari and Khayati, 2011).

Effect of temperature: To determine the effect of temperature on the activity of enzyme, the partially purified enzyme (500 μL) was mixed with 500 μL of Tris-HCl buffer (pH 8.0) and incubated at different temperatures (37, 40, 50°C). Casein substrate was added to the above mixture after 30 min and incubated at 37°C for 10 min. The reaction was stopped by the addition of TCA and the supernatant was obtained by centrifugation was measured at 280 nm (Venugopal and Saramma, 2006).

Effect of NaCl: The effect of NaCl on enzyme activity was determined by incubating the partially purified enzyme with different concentrations of NaCl (0 to 2.0 M). The residual activity of the enzyme was checked after incubation. The control without addition of NaCl was maintained (Sana et al., 2006).

Effect of inhibitors: To determine the type of enzyme, the partially purified enzyme was incubated with various enzyme inhibitors like phenylmethylsulfonyl fiuoride (PMSF), ethylenediaminetetraacetic acid (EDTA) and dithiobis-nitrobenzoic acid (DTNB). The enzyme inhibitor mixture was incubated for 30 min at 37°C, the residual activity was measured using casein as a substrate. The activity of the enzyme assayed in the absence of inhibitors was taken as 100% (Sen et al., 2011).

RESULTS AND DISCUSSION

Purification of the enzyme: The halotolerant protease was produced and the enzyme was purified through ammonium sulphate fractionation followed by ion exchange and gel permeation chromatography. Further, the purification of the enzyme was confirmed in MALDI-TOF. A summary of the purification was shown in Table 1. The ammonium sulphate fractionation was an effective step in purification which was leading to 2.1-folds purification with specific activity of 40 U mg-1. The ion exchange chromatography with DEAE Sephadex enhanced the specific activity to 63 U mg-1 with 3.3 fold purification. During the last step of purification with gel permeation chromatography the specific activity was further enhanced to 102 U mg-1 with 5.2 folds purification (Fig. 1, 2).

SDS-PAGE, zymogram and MALDI-TOF analysis: Protein purification was successfully achieved to the homogeneity which was evident by the appearance of single band corresponding to 36 kDa on SDS-PAGE (data not shown). The molecular weight was lower as compared to other halophilic and alkaline proteases where it ranged from 40 to 130 kDa (Studdert et al., 2001; Gimenez et al., 2000; Kamekura and Seno, 1990; Schmitt et al., 1990).

Table 1: Purification fold and recovery in each purification steps

Fig. 1: Elution profile of enzyme from ion exchange chromatography

The protease activity of the purified enzyme was confirmed in zymogram which clearly showed the clear zone against the substrate. The degree of purity was further confirmed by MALDI-TOF mass spectrometry, which showed a single peak with 36438.21 kDa (Fig. 3, 4).


Fig. 2: Elution profile of protease from Sephadex G-75

Fig. 3(a-b): Zymogram analysis of protease; (a) Enzyme eluted from Ion Exchange Chromatography and (b) Enzyme eluted from Sephadex G-75

Fig. 4: MALDI-TOF analysis of purified enzyme showing molecular mass of 36438.210

CHARACTERIZATION OF THE ENZYME

Effect of pH: The pH profile of the halotolerant protease was determined at 37°C by incubating the purified enzymes are different pH range (6.0-9.0). The enzyme was active in all the tested pH range and the optimum was found to be at pH 8.0 (Fig. 5). Similarly, a previous study with a protease produced by Monascus purpureus grown on marine wastes showed pH 8.0 as optimum pH (Liang et al., 2006). In contrast a study with haloalkaliphilic bacterium Halogeometricum borinquense (Vidyasagar et al., 2006), Bacillus sp. (Gupta et al., 2005), B. subtilis CN215 (Uchida et al., 2004) and B. subtilis PE-11 (Adinarayana et al., 2003) showed pH 10.0 as optimum for enzyme activity.

Effect of temperature: The optimum temperature for enzyme activity was 40°C beyond which there was a rapid decline. Similarly, at lower temperature, the enzyme activity sharply decreased (Fig. 6). This result is in accordance with Sana et al. (2006) showed 40°C is optimum for a marine bacterium. However, the temperature tolerance of this enzyme is quite lower than many halophilic proteins such as protease from halophilic bacterium Salinivibrio sp. showing optimal activity at 65°C and another report (Gupta et al., 2005) showed 60°C as optimum for an solvent tolerant bacterium Pseudomonas aeruginosa eventhough it is active from 40 to 65°C.

Fig. 5: Enzyme activity at different pH range

Fig. 6: Enzyme activity at different temperatures

Fig. 7: Enzyme activity at different percentage of sodium chloride

Table 2: Effect of inhibitors on enzyme activity

Effect of NaCl: The effect of NaCl on enzyme activity was tested in different concentrations of NaCl (0 to 2.0 M). Maximum activity was found in 1.5 M (Fig. 7). In contrast, a study with Salinivibrio strain showed maximum activity at 0.5 M (Karbalaei-Heidari et al., 2007). Further, increase in salt concentration led to reduction in activity this is in accordance with a study showed reduction in activity with increase salt concentration (Patel et al., 2006). But a study with a marine bacterium showing optimum activity at even 30% of NaCl and even it is stable at 35% (Sana et al., 2006). A study with a marine organism Halogeometricum borinquense showed activity with 30% NaCl even at an incubation temperature of 60°C (Vidyasagar et al., 2006).

Effect of inhibitors: To determine the type of enzyme, purified enzyme was incubated with different protease inhibitors. Protease showed complete inhibition against PMSF (phenylmethylsulphonyl fluoride) (Table 2). Hence, it is confirmed that this halotolerant enzyme was a serine type. PMSF sulphonated the serine active site which results in the loss of activity (Gold and Fahrney, 1964). There was no inhibition with EDTA (ethylene diamine tetraacetic acid) and DTT (dithiothreitol) which are metallo and thiol protease inhibitors. Similar results showed serine protease B. licheniformis (Tang et al., 2004), B. pumilus (Aoyama et al., 2000; Huang et al., 2003) and B. intermedius (Balaban et al., 2004).

CONCLUSION

The extracellular protease from halotolerant bacterium VITP14 was extracted and purified which was further confirmed by zymogram. Purity check and molecular weight identification was done with MALDI-TOF and SDS-PAGE. The enzyme was also characterized for its optimal and maximal activity with different pH, temperature and salt concentration. Thus, this enzyme will be much potential in industries where higher salt concentrations were used during fermentation process.

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