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Enhanced production, purification and biochemical characterization of therapeutic potential fibrinolytic enzyme from a new Bacillus flexus from marine environment

Department of Botany and Microbiology, College of Sciences, King Saud University, P.O. Box 22452, Riyadh 11495, Saudi Arabia
Bioprocess Engineering Division, Smykon Biotech Pvt LtD, Nagercoil, Kanyakumari, Tamil Nadu 629201, India

⁎Corresponding author. dfarraj@ksu.edu.sa (Dunia A. Al Farraj)

Disclaimer:
This article was originally published by Elsevier and was migrated to Scientific Scholar after the change of Publisher.

Peer review under responsibility of King Saud University.

Abstract

Objectives

The main aim of this study is to isolate and characterize fibrinolytic enzyme from Bacillus flexus.

Methods

Fish meal of Sardinella longiceps and anchovy was optimized using a two-level full factorial design (25) and response surface methodology. The significant physical factors and nutrient sources (peptone, maltose, and magnesium chloride) were identified by statistical approach. The properties of a purified enzyme including their effect at different temperature, pH and the effect of metal ions were evaluated.

Results

Enzyme yield was improved 3.5 fold than unoptimized medium. Central composite design optimized culture medium enhanced enzyme yield (4711 ± 29.3 U/g of substrate). The fibrinolytic enzyme was highly active at alkaline pH (8.0), 50 °C and the molecular weight was 32 kDa.

Conclusions

From these findings, it concludes that this fibrinolytic enzyme could be a novel potent thrombolytic agent.

Keywords

Fibrinolytic enzyme
Bacillus
Cheap substrates
Blood clot
Fibrinolytic agent
1

1 Introduction

Cardiovascular diseases (CVDs) cause high mortality throughout the World. The thrombotic disease such as ischemic heart disease, high blood pressure, and acute myocardial infarction is of great concern nowadays and still thrombolytic therapy is primary way to treat these diseases (Marder, 2009). Microorganisms have been widely known as a vital source of thrombolytic agents. It is highly essential to look for novel and safer fibrinolytic agents from other microbial sources. To overcome various drawbacks, several fibrinolytic enzymes of different bacterial origin have been studied (Sharma et al., 2020). Enzymes from marine microorganisms have various applications than conventional biocatalysts due to its high potentials at large temperature and pH ranges with the potential to catalyze numerous catalytic functions. Fibrinolytic enzymes are produced by solid state fermentation (SSF) or submerged fermentation. SSF has various advantages over submerged fermentation like higher yield, less effluent formation, simpler fermentation apparatus, less need for stringent fermentation condition, provide culture conditions similar to natural habitat of microorganisms and high enzyme yield. Bacteria preferred SSF for the production of enzymes because this process condition is similar with natural environment. The ready availability of media components and substrate cost are the essential factors in industrial production (Vijayaraghavan and Prakash Vincent, 2015). Enzyme production is greatly affected by various nutrient sources and physico-chemical factors. Response surface methodology (RSM) is a combination of various statistical approaches by analyzing the components interactions aids in predicting optimum conditions of independent variables (Deepak et al., 2008). It analyzes the effect of factors, designs experiments and builds up models for foreseeing alterations in production. RSM and two factorial designs reduce the experimental runs for a multiple number of variables, based on which high yield in the production of enzyme can be done (Mukherjee et al., 2012). Based on the above mentioned facts and criteria, in this work the marine bacteria, Bacillus flexus from marine sediments with strong fibrinolytic activity, optimized their production in SSF with fish meal as SSF substrate using RSM.

2

2 Materials and methods

2.1

2.1 Screening of organism from the marine environment

The bacterial strain was screened from South West coast of India. Sample collection was done widely along the coasts of Kanyakumari in deep water, on beaches, under docks, in coves and sampling was on algal sediments. Screening for proteases were done in skimmed milk agar plates at pH, 7.0 with the addition of 3.5% (w/v) sodium chloride to maintain natural environment. PZ value was used to identify the potent proteolytic enzyme-producing bacterial isolate (Vijayaraghavan and Vincent, 2013) and isolates with low PZ value was considered for fibrinolytic enzymes screening. Fibrin substrate plate was formed by using bovine fibrinogen and thrombin. After incubating the fibrin plate at 37 °C, 10 µL sample was inoculated into well (6 mm) and incubated for 5 h. The diameter of the area of clearing zone was estimated, which indicated enzyme activity.

2.2

2.2 Production of fibrinolytic enzyme and assay

Submerged fermentation was performed in 100 mL Erlenmeyer flask. The culture flask was incubated for two days at 175 rpm in a rotary shaker incubator. After two days enzyme was extracted. Enzyme activity was measured based on the zone of clearance around the sample well and urokinase was used as the standard.

2.3

2.3 Identification of enzyme secreting bacterium

The potent bacterium was selected based on initial screening and enzyme assay. The selected candidate organism was identified based on morphological and biochemical experiments. Further characterization of the particular organism was done based on 16S rDNA gene sequence analysis using forward primer F: 5′-AGAGTTTGATCMTGG-3 and 1492 R: 5′-ACCTTGTTACGACTT-3 reverse primer and found to be Bacillus flexus.

2.4

2.4 Screening of factors using traditional method by solid state fermentation

Fish meal refers to waste of Sardinella longiceps and anchovy. These two were dried and mixed 50:50 ratios and used as the substrate. This substrate was used for optimization studies. 5.0 gm substrate was taken and the moisture content was maintained as 70% (pH 8.0) using Tris-HCl buffer. The medium was sterilized and cooled and B. flexus was inoculated at 10% level. Further, Erlenmeyer flask was incubated for 48 h at 37 °C. The factors such as carbon sources (1%) (starch, trehalose, glucose, maltose, sucrose and xylose), nitrogen sources (1%) (beef extract, casein, peptone, gelatine, yeast extract, and urea), and inorganic ions (0.1%) (manganese chloride, magnesium chloride, sodium nitrate, disodium hydrogen phosphate, ammonium sulphate, ammonium chloride, calcium chloride) were analyzed.

2.5

2.5 Screening of variables by statistical approach

Five factors (maltose, peptone, magnesium chloride, pH, and moisture) were selected. To maintain pH of the substrate, buffer solution (0.1 M) was used at required pH. Moisture level of the medium was adjusted using suitable buffer. The selected factors were analyzed at two different levels. A total of 32 experimental runs (Table 1) were performed and the corresponding responses were estimated. The statistical software (Design-Expert 8.0.7.0) has been used to design the experiments and analyze the data.

Table 1 A two level full factorial experimental design for five variables and fibrinolytic enzyme production in SSF.
Run Maltose % Peptone % MgCl2 % pH Moisture % Enzyme activity (U/g)
1 1.00 1.00 0.01 10.0 60.0 2680
2 1.00 1.00 0.10 7.0 90.0 1197
3 0.10 1.00 0.10 7.0 60.0 2076
4 0.10 1.00 0.10 10.0 60.0 4401
5 1.00 0.10 0.01 7.0 90.0 1185
6 0.10 1.00 0.01 10.0 90.0 1152
7 0.10 0.10 0.01 7.0 60.0 2074
8 1.00 1.00 0.01 7.0 60.0 916
9 0.10 0.10 0.10 7.0 60.0 931
10 1.00 0.10 0.01 10.0 60.0 899
11 0.10 0.10 0.10 10.0 60.0 1164
12 1.00 1.00 0.10 7.0 60.0 1976
13 0.10 0.10 0.01 7.0 90.0 1398
14 0.10 0.10 0.10 10.0 90.0 1876
15 1.00 1.00 0.01 10.0 90.0 3001
16 0.10 1.00 0.10 7.0 90.0 928
17 0.10 0.10 0.10 7.0 90.0 3659
18 0.10 1.00 0.01 10.0 60.0 1153
19 0.10 1.00 0.01 7.0 90.0 897
20 1.00 0.10 0.01 10.0 90.0 1198
21 1.00 0.10 0.01 7.0 60.0 1156
22 1.00 0.10 0.10 10.0 90.0 1837
23 0.10 0.10 0.01 10.0 90.0 1829
24 0.10 0.10 0.01 10.0 60.0 1167
25 1.00 1.00 0.10 10.0 60.0 2698
26 1.00 0.10 0.10 7.0 60.0 2078
27 0.10 1.00 0.10 10.0 90.0 1157
28 1.00 1.00 0.10 10.0 90.0 4802
29 1.00 1.00 0.01 7.0 90.0 1402
30 0.10 1.00 0.01 7.0 60.0 1538
31 1.00 0.10 0.10 7.0 90.0 1109
32 1.00 0.10 0.10 10.0 60.0 939
Table 2 Analysis of variance (ANOVA) for the designed two level full factorial experiment for fibrinolytic enzyme production.
Source Sum of squares df Mean square F-value p-value
Model 3.153E+007 25 1.261E+006 113.69 <0.001
A-Maltose 87466.53 1 87466.53 7.89 0.0308
B-Peptone 1.746E+006 1 1.746E+006 157.43 <0.001
C--MgCl2 2.635E+006 1 2.635E+006 237.60 <0.0001
D-pH 1.727E+006 1 1.727+006 155.67 <0.0001
AB 2.569E+006 1 2.569E+006 231.63 <0.0001
AD 1.377E+006 1 1.377E+006 124.11 <0.0001
AE 4.993E+005 1 4.993E+005 45.01 0.0005
BC 4.534E+005 1 4.534E+005 40.88 0.0007
BD 5.116E+006 1 5.116E+006 461.27 <0.0001
BE 1.355+066 1 1.355+066 122.17 <0.0001
CD 1.811E+005 1 1.811E+005 16.32 0.0068
DE 2.214E+005 1 2.214E+005 20.86 0.0038
ABC 71347.53 1 71347.53 6.43 0.0443
ABD 4.741E+005 1 4.741E+005 42.74 0.0006
ABE 3.388E+006 1 3.388E+006 300.95 <0.0001
ADE 1.526E+006 1 1.526E+006 137.63 <0.0001
BCD 7.469E+005 1 7.469E+005 67.35 0.0002
BCE 65250.78 1 65250.78 111.37 <0.0001
CDE 65250.78 1 65250.78 5.88 0.0515
ABCD 2.157E+005 1 2.157E+005 19.44 0.0045
ABCE 2.061E+006 1 2.061E+006 185.82 <0.0001
ABDE 57715.03 1 57715.03 5.20 0.0627
ACDE 3.601E+006 1 3.601E+006 324.69 <0.0001
BCDE 1.338+005 1 1.338+005 12.06 0.0133
ABCDE 21684.03 1 21684.03 1.96 0.2115
Residual 66547.44 6 66547.44
Cor Total 3.159E+007 31

2.6

2.6 Response surface design and optimization

The independent variables such as, peptone, pH and MgCl2 were used to optimize fibrinolytic production. The level of factors (−1 and +1) with midpoint (0) and the complete experimental setup with their corresponding value is listed in Tables 3 and 4. Every experiment was conducted in three different experiments. Multiple regression analysis of the data was done and defined predicted response (Y) which is the second-order polynomial equation by virtue of independent variables (X1, X2, and X3) was found out:

Table 3 Central composite design for three variables and production of fibrinolytic enzymes in SSF.
Run pH Peptone MgCl2 Enzyme activity
% % U/g
1 7.0 1.0 0.1 1263
2 10.0 1.0 0.1 3022
3 6.0 0.6 0.6 1597
4 8.5 1.3 0.6 3904
5 8.5 0.6 0.6 4280
6 10.0 0.1 0.1 3993
7 8.5 0.6 0.6 4128
8 10.0 1.0 1.0 4086
9 8.5 0.6 0.6 4490
10 11.0 0.6 0.6 1802
11 8.5 0.6 0.2 3059
12 8.5 0.6 1.3 4029
13 8.5 0.2 0.6 2098
14 8.5 0.6 0.6 4187
15 7.0 1.0 1.0 4678
16 10.0 0.1 1.0 401
17 7.0 0.1 0.1 3278
18 7.0 0.1 1.0 1739
19 8.5 0.6 0.6 4036
20 8.5 0.6 0.6 4182
Table 4 Analysis of variance (ANOVA) for the production of fibrinolytic enzymes in SSF.
Source Sum of squares df Mean square F-value p-value
Model 2.995E+007 9 3.327E+006 49.03 <0.001
A-pH 57839.65 1 57839.65 0.85 0.3777
B-Peptone 3.263E+006 1 3.263E+006 48.08 <0.0001
C--MgCl2 70228.84 1 70228.84 1.03 <0.0001
AB 4.005E+005 1 4.005E+006 5.90 <0.0001
AC 2.424E+006 1 2.424E+006 35.72 <0.0001
BC 1.154E+007 1 1.154E+007 170.09 <0.0001
A2 1.063E+007 1 1.063E+007 156.61 <0.0001
B2 2.290E+006 1 2.290E+006 33.75 0.0002
C2 6.156E+005 1 6.156E+005 461.07 0.0131
Residual 6.787E+005 10 67868.21
Lack of Fit 5.574E+005 5 1.115E+005 4.59 0.0598
Pure Error 1.213E+005 5 24260.97
Car Total 3.062E+007 19

Y = α0 + α1A + α2B + α3C + α1α2AB + α1α3AC + α2α3BC + α1α1A2 + α2α20B2 + α3α3C2

where Y = fibrinolytic enzyme activity in U/g; A = coded value of pH; B = coded value of peptone; C = coded value of MgCl2.

The predicted experimental model was validated with experiments.

2.7

2.7 Total protein estimation

The culture supernatant was used as the sample source for the estimation of protein (Lowry et al., 1951).

2.8

2.8 Enzyme purification

Enzyme secreted by B. flexus was centrifuged and filtered using filter unit. The crude sample was precipitated with ammonium sulphate at three different saturations (20%, 40% and 60%). The precipitated enzyme was suspended in Millipore water and the precipitated enzyme was dialyzed. The overnight dialyzed enzyme was further dialyzed against buffer A (Tris-HCl buffer, 25 mM, pH 8.0) and lyophilized (Balaraman and Prabakaran, 2007). The lyophilized sample was fractionated using a sephadex G-100 chromatography column. About 25 fractions were collected and enzyme activity was determined. Fibrinolytic enzyme fractions were pooled and lyophilized. The freeze dried sample was mixed with buffer A and determined molecular weight using sodium dedecyl sulphate (SDS)-PAGE (Laemmli, 1970).

2.9

2.9 Characterization of enzyme

Optimal temperature of the fibrinolytic protease was found by analyzing the enzyme activity and stability at temperature ranges between 30 and 70 °C. Enzyme stability was performed for 1 h at pH 8.0. Impact of pH on enzyme activity was analyzed using buffers at ranges between 3.0 and 10.0 (Al-Dhabi et al., 2020). pH stability was determined by treating sample for 60 min at a definite temperature (50 °C) for 60 min and enzyme stability was calculated (Taneja et al., 2017). The impact of metal ions (5 mM) was tested using Ca2+, Cu2+, Co2+, Fe2+, Hg2+, Mn2+, Mg2+, Na+ and Zn2+. The influence of inhibiting properties of enzyme was studied by substituting 1–5 mM phenylmethylsulfonyl fluoride (PMSF) with fibrin plate and enzyme assay was performed as described earlier (Shinde et al., 2012).

3

3 Results and discussion

3.1

3.1 Screening and characterization of the Bacillus flexus for fibrinolytic enzyme production

In this study, 33 strains were screened from diverse sources in the marine habitats. PZ value was found to be much less for Bacillus flexus (0.18) which indicated good protease production. Further, the maximum protease producing 10 bacterial strains were used for screening fibrinolytic enzyme production using fibrin-agarose plates. The selected bacterial strain showed 23 mm zone around the well indicated hyper production. The isolate was Gram-positive, catalase-, Vogues-Proskauer’s test, methyl red, indole tests were negative and positive to oxidase experiment. It was unable to hydrolyze urea, nitrate was reduced and citrate was utilized. Based on 16S rDNA sequencing, the organism was characterized as B. flexus.

3.2

3.2 Optimization of fibrinolytic enzyme production by traditional method

. Bacterial proteolytic activity predominantly based on the composition of culture media for growth and various physical entities. However, the optimum conditions of the medium differ among organisms (Vijayaraghavan and Vincent, 2012). The selected strain could utilize maltose (1023 ± 15 U/g) improved enzymes production, closely followed by the one which is supplemented with starch (987 ± 14 U/g) with considerable decrease in fibrinolytic activity when supplemented with glucose. All nitrogen sources increased enzyme production with peptone (952 U/g) in the medium increases enzyme production the most followed by gelatin (949 U/g) and casein (938 U/g). The enzyme production was 1.2 fold higher when the medium was supplemented with MgCl2 (863 U/g) and also shows significant increase in enzyme production when supplemented with CaCl2 (860 U/g), and Na2HPO4.

3.3

3.3 Analysis of variables by statistical method

Five most significant variables (maltose (A), peptone (B), MgCl2 (C), pH (D), and Moisture (E)) were selected for enzyme production using statistical approach. The enzyme yield varied from 897 to 4802 U/g (Table 1). The important effects, each factors and their corresponding Fvalue, and Pvalue are given in Table 2. As per ANOVA results, all five variables namelyA, B, C, D, and E were effective on enzymes production. All three coefficients (quadratic, interactive and linear) namely AB, AD, AE, B C, BD, B E, DE, C D, AB C, ABD, AB E, AD E, B C E, B CD, A B C D, A B C E, AC D Eand BCDE were significant. The predicted R2 of this model design was 0.9401 and the adjusted R2 value was 0.9891. F-Value 113.69 shows the model is significant and the regression equation involving the coded variables is

Enzyme activity = +1764.78 + 52.28*A + 233.59*B + 286.97* C + 232.28*D + 283.34* AB + 207.41* AD + 124.91*AE +119.03BC + 399.84*BD-205.78*BE + 75.22*CD6*CDE + 85.03*DE-47.22* ABC + 121.72* ABD + 322.97*ABE + 218.41*ADE + 152.78*BCD-196.47*BCE-45.16*CDE-82.09*ABCD + 253.78*ABCE + 42.87*ABDE + 335.47*ACDE + 64.66 *BCDE + 26.03*ABCDE

3.4

3.4 Response surface methodology

In this study, the CCD model was statistically significant (p < 0.001). Maltose (A), peptone (B) and MgCl2 (C) variables were used for analysis. In experiment 15, maximum activity (4678 U/ml) was registered (Table 3). The F-value of this model was 49.03 and the calculated p value was <0.001 (Table 4). The R2 of this model was 0.9778 indicated the suitability of the model and the adjusted R2 value was close to the predicted correlation coefficient (0.8556). This model is fitted for the second-order polynomial equation.

Enzyme activity = +4212.37 + 65.08*A + 488*B + 7 1.71*C + 223.75*AB-550.50*AC + 1201.25*BC-858.80*A2-398.65B2-206.68*C2

The generated 3D graphs (Fig. 1A–C) represent the interaction among the medium components and the determined components optimum for maximum enzyme yield. The perturbation plot revealed the impact of all factors simply (Fig. 1D). The increasing concentration of MgCl2 and peptone positively regulated enzymes production. The optimized value of three most important factors was 0.4% MgCl2, 0.92% peptone, at pH 8.2% with predicted estimate of 4692 U/g fibrinolytic activity. The predicted results were confirmed by performing experiments in triplicates under optimized conditions and enzyme activity achieved was 4711 U/g. CCD and RSM have been used frequently to optimize enzymes production and there are few other reports of increasing fibrinolytic enzyme production using RSM (Mukherjee et al., 2012). Enzyme yield was improved 3.5 fold than unoptimized medium and this yield was comparatively high than various previous reports (Deepak et al., 2008; Vijayaraghavan and Vincent, 2014). Comparison with all these strains of Bacillus the present isolate marine B. flexus also had shown increased enzymes production.

(A–D). Response surface plots showing interaction between process variables for enhanced production of fibrinolytic enzymes from B. flexus (A) pH and peptone (B) pH MgCl2 (C) peptone and MgCl2 (D) perturbation plot.
Fig. 1
(A–D). Response surface plots showing interaction between process variables for enhanced production of fibrinolytic enzymes from B. flexus (A) pH and peptone (B) pH MgCl2 (C) peptone and MgCl2 (D) perturbation plot.

3.5

3.5 Properties of fibrinolytic enzyme

Enzyme was purified by and molecular weight of enzyme was analyzed using SDS-PAGE (Fig. 2) and determined as 32 kDa. The final purification was 10.8-fold with the estimated recovery of 10%. The molecular weight of fibrinolytic enzyme was comparatively higher than fibrinolytic enzymes from other sources (Simkhada et al., 2010. Also, the molecular weight of the enzyme is significantly high but comparatively lower than plasminogenic activator. The specific activity of fibrinolytic enzyme was 315.2 U/mg protein (Table 5).

Molecular weight determination using 12% SDS-PAGE (Lane 1 – purified sample, Lane 2 – ammonium sulphate precipitated sample; lane – 3 crude sample).
Fig. 2
Molecular weight determination using 12% SDS-PAGE (Lane 1 – purified sample, Lane 2 – ammonium sulphate precipitated sample; lane – 3 crude sample).
Table 5 Purification summary of fibrinolytic enzyme secreted by B. flexus.
Purification steps Total activity (U) Total protein (mg) Specific activity (U/mg) Purification (fold) Yield (%)
Crude enzyme 12,800 212 60.6 1 100
Ammonium sulphate
precipitation 9750 145.3 67.1 1.1 76.2
Sephadex G-75 1387 4.4 315.2 5.2 10.8

3.6

3.6 Characterization of enzyme

The enzyme activity and stability was both at its highest at pH 8 and was generally active at pH range of 7 to 9 (Fig. 3A). Enzyme was highly active at 50° C but enzyme stability drastically decreases at 70 °C (Fig. 3B). Fibrinolytic enzyme under study was found to be active at pH 8.0 and 60 °C. This optimum temperature obtained in this study was high than some previous reports (Liu et al., 2005). In the case of Bacillus subtilis C10, fibrinolytic enzyme was active between 31 and 43 °C (Thu et al., 2020). Also preservation under normal condition is possible with its high optimal temperature and temperature stability. Recently, Yao et al. (2019) isolated a fibrinolytic enzyme producing Bacillus velezensis BS2 from sea squirt jeotgal. The fibrinolytic enzyme isolated from this organism showed high activity at 37 °C. Inhibition and activation studies on enzyme can give finer details about the origin of enzymes (Mukherjee and Rai, 2011). In a study, Sharma et al. (2020) characterized a thiol-dependent fibrinolytic enzyme from Bacillus cereus RSA1 for therapeutic applications. Mg2+ is one of the significant ions enhanced fibrinolytic enzyme activity which was also enhanced enzymes production. Zn2+, Fe2+ and Hg2+ inhibited the enzyme activity drastically (Fig. 3C). Enzyme activity of the enzyme was higher with Mg2+ and Mn2+ ions and was mildly enhanced by Ca2+ was like Brevibacillum sp. serine metallo proteases (Maeda et al., 2011), and these indicates that these ions may exist in the enzyme.

(A–C). Effect of pH on enzyme activity and stability (A), Effect of temperature on enzyme activity and stability (B), Effect of ions on enzyme activity (C).
Fig. 3
(A–C). Effect of pH on enzyme activity and stability (A), Effect of temperature on enzyme activity and stability (B), Effect of ions on enzyme activity (C).

4

4 Conclusion

Fibrinolytic enzyme production in hyper-producing novel strain B. flexus has been utilized. The utilization of inexpensive meal and statistical design of culture conditions in screening and optimization allowed identification of significant factors instantly and their interactions for fibrinolytic enzyme. The present finding has illustrated the application of central composite design by predicting conditions enabling maximum enzyme yield. The present study indicated that this fibrinolytic enzyme from this bacterium can be used efficiently as a fibrinolytic agent.

Acknowledgement

The authors would like to thank the Deanship of Scientific Research at King Saud University for funding this work through research group no. RG1439-044.

Declaration of Competing Interest

The authors declare that they have no known competing financial interests or personal relationships that could have appeared to influence the work reported in this paper.

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