Effective extraction of elastase from Bacillus sp. fermentation broth using aqueous two-phase system

Effective extraction of elastase from Bacillus sp. fermentation broth using aqueous two-phase system 1 2 first-author 1 corresp ‡Corresponding Author ‡Corresponding Author †E-mail:gqhe@zju.edu.cn †E-mail:gqhe@zju.edu.cn gqhe@zju.edu.cn 3 Department of Food Science and Nutrition, Zhejiang University, Hangzhou 310029, China Department of Food Science and Nutrition, Zhejiang University, Hangzhou 310029, China School of Food Science and Engineering, Ocean University of China, Qingdao 266003, China School of Food Science and Engineering, Ocean University of China, Qingdao 266003, China School of Food Science and Technology, Southern Yangtze University, Wuxi 214036, China School of Food Science and Technology, Southern Yangtze University, Wuxi 214036, China This paper presents the evaluation of an aqueous two-phase system (ATPS) for extracting elastase produced by Bacillus sp. EL31410. The elastase and cell partition behavio r in polyethylene glycol (PEG)/salt systems was investigated. The suitable system for elastase extraction was PEG/KH 2 PO 4 -K 2 HPO 4 , in which elastase is mainly partitioned into the PEG-rich phase, while the cells remained in the other phase. The influence of defined system parameters (e.g. PEG molecular mass, pH, NaCl addition) on the partitioning behavior of elastase is described. The concentration of phase forming components, PEG and KH 2 PO 4 -K 2 HPO 4 , was optimized for elastase recovery by means of response surface methodology, and it was found that they greatly influenced extraction recovery. The optimal ATPS was 23.1% ( w / w ) PEG 2 000 and 11.7% ( w / w ) KH 2 PO 4 -K 2 HPO 4 . The predicted recovery was about 89.5%, so this process is suggested to be a rapid and convenient method for elastase extraction. Elastase Aqueous two-phase system (ATPS) Bioseparation Purification Optimization Response surface methodology (RSM) INTRODUCTION 1 Aqueous two-phase system (ATPS) is widely used in biochemistry and biotechnology for purification of proteins (Diamond and Hsu, 1992 1992 ; Balasubramaniam et al., 2003 2003 ), enzymes (Pan et al., 2001 2001 ; Bim and Franco, 2000 2000 ), amino acids (Li et al., 2002 2002 ), antibiotics (Yang et al., 1994 1994 ; Guan et al., 1994 1994 ), nucleic acids (Ohlsson et al., 1978 1978 ; Kimura, 2000 2000 ), aroma compounds (Marco et al., 2000 2000 ) and lactic acid (Planas et al., 1998 1998 ). ATPS is mainly composed of two-incompatible polymers (e.g. Dextran/PEG) or a polymer and a salt (usually phosphate and sulfate) and has great potential for industrial applications because it can be used to obtain a concentrated and purified product in one step by addition of crude broths containing suspended matter (e.g. cells), and offers gentle nontoxic environments for labile biomolecules. Well-known advantages of ATPS are volume reduction, high capacity, rapid separations, easy scale-up and suitability for continuous large-scale operations (Yan, 2001 2001 ). PEG/salt systems, especially, are widely applied for bioseparation of proteins because of their low cost and wide range of hydrophobicity differences between the two-phase systems (Li et al., 2001 2001 ). The uneven partitioning of a protein in ATPS depends not only on the surface properties (such as the size, charge and hydrophobicity) of the protein but also on the physicochemical traits of the two phases. The nature of the system is influenced by changing factors such as polymers, polymer molecular mass and concentration, the type of phase forming salt and its concentration, NaCl concentration as well as the pH of the system. The partition of compounds in these systems is very complex due to several factors, including hydrogen bonds, charge, hydrophobic interactions and static effects. The mechanisms still remain unclear for this kind of uneven partitioning of materials. For a particular application, experimentation is necessary to define an optimal system. Elastase is a protease that catalyzes the hydrolysis of elastin (Morihara, 1967 1967 ), and is widely applied in biochemical medicine, as a tenderizer for meat in the food industry, in cosmetics, and in environmental protection. When compared to extraction of elastase from pancreatic tissue, production by fermentation technology is more promising due to its low cost, high production rate, and readily controlled conditions. To date, research has been concentrated on isolation and screening of microorganisms that produce elastase, and on the purification and characterization of newly found enzymes (Shibata et al., 1993 1993 ; Tsai et al., 1988 1988 ; Michelle et al., 2001 2001 ). Bioseparation protocols reported were conventional methods such as centrifugation followed by fractional precipitation and chromatography. ATPS seems to be a good alternative to a first step purification as this allows the removal of several contaminants. However, the possibility of use of the ATPS process for the recovery of elastase is not documented. We recently reported an elastase producing strain Bacillus sp. EL31410, with strong powerful ability for elastase production, and the cultivation parameters (Chen et al., 2002 2002 ; He et al., 2004 2004 ). This study aimed at investigating the factors affecting elastase partition in PEG/salt and optimizing the ATPS components using response surface methodology (RSM), and finding a more suitable system to develop the ATPS process for elastase recovery and purification. MATERIALS AND METHODS 1 Materials 2 Polyethylene glycol (PEG) 400, 600, 1 000, 4 000, 6 000 were purchased from Shanghai Pudong Gaonan Chemical Company (Shanghai, China). PEG 2 000 was produced by China Medicine Shanghai Chemical Company (Shanghai, China). The salts and other chemicals used were of analytical grade. Bacterial strains, media and cultivation 2 Bacillus sp. EL31410 was screened and preserved by Microbiology Lab of Department of Food Science and Nutrition, Zhejiang University, China. The stock culture was maintained at 4 °C on agar slants containing (g/L) 4 beef extract, 6 peptone, 2 yeast extract, 5 NaCl and 20 agar (initial pH 7.5). The growth medium for seed culture was the same as that for the stock culture with the exception of agar. The fermentation medium consisted of (g/L) 74 glucose, 11.3 casein, 6.16 corn liquid steep, 2.06 K 2 HPO 4 ·3H 2 O, and 0.34 MgSO 4 ·7H 2 O (initial pH 7.5). The test microorganism was inoculated into 25 ml seed medium in 250 ml Erlenmeyer flasks. For the preparation of starter cultures, cultivation was for 18 h at 37 °C on a 200 r/min rotary shaker. Elastase fermentation was carried out in a 5-L bioreactor at 30 °C and 300 r/min. Inoculation size was 4%, the loading coefficient 0.6, air flux 1 vvm, initial pH value 7.5. After cultivation, the culture was harvested and centrifuged at 3000 r/min for 15 min to obtain a yellowish supernatant. Aqueous two-phase system 2 Phase systems were prepared in a 25 ml beaker by adding appropriate amounts of PEG, stock salt(s) solution, and fermentation supernatant. The systems were adjusted to the required pH with buffer and distilled water was added to attain make up 15 g. Systems were thoroughly mixed by magnetic mixer. Properly proportioned ATPS (10 g) was weighed into a 10 ml graduated centrifuge tube, and then centrifuged at 2000 r/min for 10 min to expedite the phase separation. The centrifuged sample was placed into a water bath (25 °C) and allowed to stand for 30 min. After the phase volumes were measured, the top and bottom phases were separately withdrawn. Parameters evaluated included: (1) Recovery of elastase ( Y ) was defined as the sum of the elastase activity in the top/initial elastase activity added into the whole system. Y =100× C t V t / C o V o where C t and C o denote the measured activity units per ml (units/ml) in the top phase and the original adding samples, respectively; V t and V o are the volumes of the top phase and the original sample, respectively; (2) The partition coefficient of cell and elastase was K cell and K elastase , respectively. The ratio of biomass in both the top phase and the bottom phase was named as K cell ; the ratio of measured elastase activity in the top and that in bottom phase was defined as K elastase ; (3) Purification factor (PF) was defined as SA t / SA ori , where SA t and SA ori are the specific activities of elastase in the top and in the original supernatant, respectively. Assays 2 Elastolytic activity was assayed by the colorimetric method of Sachar ( 1955 1955 ). The reaction mixture contained congo-red elastin (20 mg), 1 ml of distilled water, 2 ml of boric acid buffer (0.2 mol/L, pH 7.4) and 1 ml of suitably diluted enzyme. The reaction mixture was incubated at 37 °C and 100 r/min for 20 min. The reaction was terminated after 20 min by adding 2 ml of sodium phosphate buffer (0.7 mol/L, pH 6.0), and immediately filtered. The absorbance of the filtrate was read at 495 nm against a control (no enzyme). One unit of elastase activity was defined as the amount of enzyme required to solubilize 20 mg of elastin-congo red under the test conditions. The protein content was determined by Bradford method using bovine serum albumin (BSA) as the standard (Bradford, 1976 1976 ). The cell content was evaluated at 600 nm by spectrophotometer. Experimental design 2 A 2 2 full factorial design (FFD) yielding four sets of experiments was used to verify the most significant factors affecting elastase recovery. On the basis of the first-order model obtained by the FFD, trails were obtained in the direction of steepest ascent. In order to fit the empirical second-order polynomial model, a central composite design (CCD) with five coded levels was implemented. The quadratic model for predicting the optimum is expressed by the following equation: $$Y = b_0 + b_1 x_1 + b_2 x_2 + b_{11} x_1^2 + b_{12} x_1 x_2 + b_{22} x_2^2$$ , where Y is the response variable, b is the regression coefficient, and x is the coded level of the independent variable. A full second-order polynomial model obtained by multiple regression technique for two factors using SAS (SAS Institute Inc. Cary, NC, USA) was used to describe the response surface. Response surface methodology (RSM), first documented by Box and Wilson ( 1951 1951 ), has proved to be a very efficient tool for optimization (Box and Hunter, 1978 1978 ). RESULTS AND DISCUSSION 1 Effects of phase-forming salt on elastase partition 2 The selection of salt used in the extraction system was one of the key points of this ATPS technique. Four different inorganic salts were evaluated. A film of sediment was observed at the interface of two phases. The results are summarized in Table 1 1 . After separation and centrifugation, the cells readily entered into the bottom phase or precipitated at the interface according to the partition coefficient, especially in PEG/KH 2 PO 4 -K 2 HPO 4 ; Recoveries of elastase for each system (PEG/(NH 4 ) 2 SO 4 , PEG/K 2 HPO 4 and PEG/KH 2 PO 4 -K 2 HPO 4 ), were higher than 50%, which suggested that elastase is favorably distributed to some degree into the top phase. For PEG/KH 2 PO 4 -K 2 HPO 4 , the elastase recovery of 75.4% and K elastase recovery of 11.73 were the highest. Partitioning of the elastase was affected by the traits of the ATPSs. The interaction of a compound with each of the phases in these systems is very complex due to the several factors involved, such as hydrophobic interactions, hydrogen bonds, charge and steric effects in a mainly surface dependent process (Marcos et al., 2002 2002 ). It should be pointed out, however, that the complexity of ATPSs is perhaps even greater because these factors are not absolutely mutually independent. Hydrophobicity is changed by the type of polymer and its relative molecular weight, concentration, as well as the salt concentration and pH. However, the values of purification factor observed were not high. It is not advisable to consider the recovery and purification factor in a biochemical method as a signal. In this work, high recovery was our goal, because ATPS is not the last purification step in elastase preparation. The PEG/KH 2 PO 4 -K 2 HPO 4 system is favorably considered for subsequent study. Each ATPS was composed of 20% ( w / w ) PEG 2000 and 13.2% ( w / w ) inorganic salt at pH 7.5; After elastase recovery, experiments were conducted to estimate the experimental error stand for the significant difference between each treatment as revealed by Duncan’s multiple range test ( P =0.05) stand for the significant difference between each treatment as revealed by Duncan’s multiple range test ( P =0.05) stand for the significant difference between each treatment as revealed by Duncan’s multiple range test ( P =0.05) Salts Recovery of elastase (%) K elastase K cell Purification factor MgSO 4 ·7H 2 O 43.6±3.0 c c 2.84 1.27 1.23±0.05 (NH 4 ) 2 SO 4 65.0±2.9 b b 6.88 1.90 1.22±0.09 K 2 HPO 4 64.4±2.0 b b 9.34 0.51 0.74±0.03 KH 2 PO 4 -K 2 HPO 4 77.9±2.4 a a 11.73 0.26 1.17±0.08 Effects of pH on elastase partition 2 The partition behaviors of elastase in systems with different pH values were studied in PEG/KH 2 PO 4 -K 2 HPO 4 system containing 20% ( w / w ) PEG 2 000 and 13.2% ( w / w ) KH 2 PO 4 -K 2 HPO 4 . Fig. 1 1 shows the partition variation over the pH range 6~11. As pH increased, the recovery of elastase decreased, especially for pH higher than 8.5. The suitable pH range was 7.0~7.7 for elastase extraction using this ATPS. The pH affected not only the targeted enzyme but also the electric traits and surface character of contaminating proteins, influenced their partition into the top and bottom phases. In addition, the ion partition proportion in the ATPS was changed, and this altered the voltage difference in-between two phases. The change of purification factor changed with the recovery, but it was still not very high. Effects of PEGs molecular weight on elastase partition 2 Using the above results, the 20% ( w / w ) PEG/13.2% ( w / w ) KH 2 PO 4 -K 2 HPO 4 (pH 7.5) was chosen for further study. The effects of various PEGs with different degree of polymerization on the partitioning of elastase are shown in Fig. 2 2 . As anticipated, the very low molecular weight (MR) of PEGs MR (400, 600) and the much higher PEGs MR (6 000) were not helpful for obtaining good elastase partitioning. At the extreme PEG MRs (400, 600 or 20 000), neither the addition of NaCl nor pH modification affected the separation process (Héctor et al., 1995 1995 ). Thus the Y -value at the top phase of the PEG 400 system was lower than that of PEG 600 for the hydrophobic protein. An increase in the MR of one of the phase polymers would cause the biomaterial to partition more strongly into the other phase. However, the magnitude of this effect decreases with increasing polymer chain length (Tanuja et al., 1997 1997 ). As the MR increases (to 1 000 and 2 000), the hydrophobicity increases correspondingly, which resulted in more elastase entering into PEG-rich phase. But as the PEG MR increased from 2 000 to 6 000, the recovery decreased significantly from 80.7% to 71.8%. This can possibly be attributed to the increase in spatial resistance with the increase of PEG MR. The higher PEGs MRs (4 000, 6 000) hindered the movement of elastase distributing into the top phase. The PEG MR influenced the targeted protein partitioning both by altering the phase diagram (i.e. by influencing the composition of the phases) and by changing the number of polymer-enzyme interactions in general. Similar phenomena were observed by others (Tanuja et al., 1997 1997 ; Baskir et al., 1989 1989 ). Purification factor also changed with the recovery but was still less than 2. The best choice of PEG for the two-phase system was PEG 2 000, which exhibited the highest partition ratio and moderate purification factor. Effect of NaCl concentration on elastase partitioning 2 The influence of NaCl concentration on the partitioning behavior of elastase was tested in ATPS containing 20% ( w / w ) PEG 2 000/13.2% ( w / w ) KH 2 PO 4 -K 2 HPO 4 (pH 7.5). As can be seen in Fig. 3 3 , when NaCl concentration increased from 0 to 10%, the recovery decreased form 80% to 35%. The elastase distribution pattern observed in these systems showed that increasing NaCl concentration beyond 2% could dramatically decrease the recovery. Although adding NaCl has been reported to be beneficial to targeted products (Silgia et al., 2000 2000 ; Cascone et al., 1991 1991 ; Marcos et al., 2002 2002 ), in the current study addition of NaCl negatively influenced partitioning of elastase into the top phase. Others described similar results in other systems (Li and He, 1992 1992 ; Isabel del-Val and Cristina, 2003 2003 ). The purification factor (PF) value was a little higher (1.54) in the system containing 2.0% NaCl than in other trails, but it was not significantly adjusted. Based on the above, NaCl will be excluded from subsequent studies. Full factorial design (FFD) of PEG and KH 2 PO 4 -K 2 HPO 4 concentration and analysis 2 The 2 2 factorial design and the results are presented in Table 2 2 . Data obtained by this design were used to derive an equation describing correlation between the independent variables and the dependent variable. The model is as follows: Y =74.07+12.75 x 1 −6.15 x 2 Analysis of variance (ANOVA) in Table 3 3 showed that the factors PEG 2 000 and KH 2 PO 4 -K 2 HPO 4 concentration were significant for P < 0.01 and P < 0.1, respectively. This verified that both two variables were important factors influencing the distribution of elastase. Increasing the concentration of PEG 2000 and decreasing that of KH 2 PO 4 -K 2 HPO 4 , according to the signs of their main effects, should have a positive impact on elastase recovery. The coefficient of determination, R 2 (determinant coefficient)=0.827, and F =14.34 ( > F 2, 6, 0.01=10.9) verified that the model was valid at probability level of 99%. The results of t -test for variance between the observed average of two-level experiment and the center point showed that the difference was not significant. This result indicated that optimum point was not in the scope of our experiment. Experimentation on the steepest ascent path was necessary to reach optimum domain. X 1 : Concentration of PEG 2 000, % ( w / w ); X 2 : Concentration of KH 2 PO 4 -K 2 HPO 4 , % ( w / w ); Y : Recovery of elastase (%) 2 No. 2 Coded level 2 Real values 2 Y (%) x 1 x 2 X 1 (%) X 2 (%) 1 −1 −1 15 10 63.1 2 1 −1 25 10 87.8 3 −1 1 15 20 50.0 4 1 1 25 20 76.3 5 0 0 20 15 80.5 6 0 0 20 15 76.8 7 0 0 20 15 79.2 8 0 0 20 15 77.5 9 0 0 20 15 78.4 Steepest ascent experiment on PEG and KH 2 PO 4 -K 2 HPO 4 concentration and analysis 2 Results shown in Table 2 2 and Table 3 3 indicated obviously that the optimal region was outside the current design space. Under this situation, a directional search method, like the steepest ascent, can be carried out to determine the next set of experiments. Based on the first-order model equation (Eq.( 3 3 )), the path of steepest ascent was aimed at increasing the concentrations of PEG 2 000 and decreasing that of KH 2 PO 4 -K 2 HPO 4 in order to improve elastase recovery. The values of elastase recovery and purification factor in these experiments are listed in Table 4 4 . The data clearly suggested that the recovery of elastase increased when the PEG concentration ( X 1 ) increased and KH 2 PO 4 -K 2 HPO 4 concentration ( X 2 ) decreased both by 0.8% (Trails No. 10 to No. 14). However, after the fourth step on the path, further experimentation could not increase the recovery. It obviously appeared that the recovery plateau occurred in the fourth step. These data showed that the results were approaching the neighborhood of optimum recovery. This composition of ATPS was chosen for the subsequent experiments. Term Parameter estimate Standard error T for H0: Parameter=0 Prob>|T| Intercept 74.07 1.76 42.029 0.0001 x 1 12.75 2.64 4.823 0.0029 x 2 −6.15 2.64 −2.327 0.0589 Root MSE 5.29 R -square 0.827 Dep mean 74.07 Adj R -square 0.769 C . V . 7.138 X 1 : Concentration of PEG 2 000, % ( w / w ); X 2 : Concentration of KH 2 PO 4 -K 2 HPO 4 , % ( w / w ); Y : Recovery of elastase (%) No. X 1 (%) X 2 (%) Y (%) 10 20.8 14.2 77.6 11 21.6 13.4 80.9 12 22.4 12.6 82.3 13 23.2 11.8 85.7 14 24.0 11.0 81.8 15 24.8 10.2 78.0 Central composite design and response surface analysis for optimization of PEG and KH 2 PO 4 -K 2 HPO 4 concentration 2 A response surface design was appropriate when the optimal region for running the course has been identified. Further optimization of elastase recovery was carried out by using a Box-Wilson central composite design with four star points and five replicates at center point for each of two factors (Box and Wilson, 1951 1951 ). Table 5 5 presents the design of this experiment and the results. Regression analysis was conducted to fit the response function with the experimental data. In order to check the statistical significance of the second-order model equation, F -test (ANOVA) was done and data shown in Table 6 6 . The value of R 2 of the polynomial model ( R 2 =0.9455) showed that 95% of the variability in the response could be explained by the model (Eq.( 4 4 )). So the Eq.( 4 4 ) was a suitable model of elastase in ATPS as measured by the recovery. The highest elastase recovery possible was determined by the confirmation of the maximum of the model. Also, Eq.( 4 4 ) showed that the signs of b 11 , b 12 and b 22 were all negative and that the parabolas open downward and have a maximum point. The ANOVA results proved that this model was appropriate. Additional, ANOVA analysis suggested that the recovery of elastase was primarily determined by the quadratic terms PEG 2 000 and KH 2 PO 4 -K 2 HPO 4 of the model, and also indicated that no significant interaction existed between the two factors. $$Y = 89.38 - 1.05x_1 - 1.97x_2 - 7.24x_1^2 - 2.18x_1 x_2 - 11.72x_2^2$$ The three-dimensional graph obtained from the calculated response surface is shown in Fig. 4 4 . The three-dimensional response surface profile of PEG 2-000 and KH 2 PO 4 -K 2 HPO 4 concentrations against recovery of elastase can further explain clearly the results of the statistical and mathematical analyses. It was evident from the plot that recovery of elastase reached its maximum at a combination of coded level −0.043 ( x 1 ) and −0.055 ( x 2 ). This reconfirms that the fitted surface has a maximum point that was 23.1% for PEG 2 000 and 11.7% for KH 2 PO 4 -K 2 HPO 4 . The model predicted a maximum response of 89.5% for this peak. In order to validate these results, experimental validations were done using a system involving this maximum point, and an average recovery value of 89.9% ( N =4) was obtained. The good correlation between these two results confirmed the validity of the response model and the model was proven to be adequate. However, purification factor (average value 1.7) still needs to be improved. The corresponding experimentations are being researched further. X 1 : Concentration % ( w / w ) of PEG 2 000; X 2 : Concentration % ( w / w ) of KH 2 PO 4 -K 2 HPO 4 ; Y : Recovery of elastase (%); x 1 =( X 1 −23.2)/2.0; x 2 =( X 2 −11.8)/2.0. The experiments were conducted in triplicate, with Y being the average value 2 No. 2 Coded level 2 Real values 2 Y (%) x 1 x 2 X 1 X 2 16 −1 −1 21.2 9.8 71.2 17 1 −1 25.2 9.8 76.8 18 −1 1 21.2 13.8 72.9 19 1 1 25.2 13.8 69.8 20 −1.41421 0 20.4 11.8 76.5 21 1.41421 0 26.0 11.8 68.8 22 0 −1.41421 23.2 9.0 67.4 23 0 1.41421 23.2 14.6 60.0 24 0 0 23.2 11.8 89.8 25 0 0 23.2 11.8 87.6 26 0 0 23.2 11.8 90.6 27 0 0 23.2 11.8 88.9 28 0 0 23.2 11.8 90.0 Regression DF Type I sum of squares R -square F -ratio Prob > F Linear 2 39.9 0.0303 1.95 0.2128 Quadratic 2 1185.6 0.9009 57.88 0.0000 Cross product 1 18.9 0.0144 1.85 0.2162 Total regress 5 1244.4 0.9455 24.30 0.0003 CONCLUSION 1 A simple process for extraction and purification of elastase from Bacillus sp. EL31410 fermentation culture was developed. Extraction of elastase in PEG/salt ATPS with high recovery was successfully proved to be a rapid and convenient method that integrated elastase extraction with cell removal. This procedure of extracting elastase using PEG/salt ATPS is an economic approach to large-scale elastase recovery. Statistical experimental designs proved to be useful tools in optimizing elastase extraction in PEG/salt ATPS. The system compositions, PEG 2 000 and KH 2 PO 4 -K 2 HPO 4 , strongly affected elastase recovery. The optimal ATPS for elastase extraction from the culture was 23.1% ( w / w ) PEG 2 000 and 11.7% ( w / w ) KH 2 PO 4 -K 2 HPO 4 at pH 7.5. In addition to establishing optimal extraction parameters for process operation, the present methodology also makes it possible to predict the elastase recovery when the system is disturbed in some way. References D Balasubramaniam , C Wilkinson , KV Cott , CM Zhang . Tobacco protein separation by aqueous two-phase extraction . J Chromatogr A , 2003 . 989 119 - 129 . DOI: 10.1016/S0021-9673(02)01900-3 http://doi.org/10.1016/S0021-9673(02)01900-3 . 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Extraction of Cephalosporin C from whole broth and separation of desacetyl Cephalosporin C by aqueous two-phase partition 10.1631/jzus.2005.B1087 Project (No. 20276064) supported by the National Natural Science Foundation of China 2005-06-07 2005-09-03 2005-10-28 2022-01-05 Copyright © 2005, Journal of Zhejiang University Science 2005 Journal of Zhejiang University-SCIENCE B (Biomedicine and Biotechnology) 11 6B