Statistical study for enhanced production of CMCase by RSM
The statistical response surface methodology (RSM) is a useful model for studying the effect of several factors influencing the process of enzyme production. Therefore, the RSM study was conducted using the Central Composite Design (CCD) of experiments for bacterial strain of Bacillus sp. NAB37. The four independent variables chosen were temperature (oC) (A), pH (B), concentration of substrate (pretreated biomass) (%w/v) (C) and concentration of starch (%w/v) (D). Each variable was set at two levels (-1 and + 1). The minimum and maximum ranges of variables have been listed in Table 1. A set of 30 experiments was carried out (Table 2). The analysis of variance (ANOVA) yielded the following regression equation in terms of the CMCase enzyme production (Y1) as a function of temperature (A), pH (B), substrate concentration (C) and concentration of starch (D):
Y1 = 3.45 − 0.083 × A – 0.087 × B + 0.65 × C + 0.10 × D + 4.250E-003 × AB − 0.16 × AC + -0.013 × AD − 0.074 × BC − 0.018 × BD + 0.030 × CD − 0.60 × A2 − 0.49 × B2 + 0.097 × C2 − 0.52 × D2 (2)
The mean predicted response based on above polynomial equation and the observed responses have been shown in Table 2. As shown in Table 3, ANOVA of regression model indicated the value of determination coefficient (R2) to be 0.9938, which implies that 99.38% of the experimental data of the CMCase production was compatible with the data predicted by the model. The R2 value is always between 0 and 1.0. An R2 value closer to 1.0 shows that the model is stronger. The value of the adjusted determination coefficient (adjusted R2) was 0.9881, which indicates greater significance of the model. A low value of coefficient of variation (C.V., 5.60%) demonstrated better precision and reliability of the executed experiments. The adequate precision value measures signal to noise ratio, and a ratio > 4.0 is desirable. In the present model, higher ratio of 52.229 indicated an adequate signal, and also proved that model could be used to navigate the design space. The F-value of 172.41 denotes that the model was significant. There is only 0.01% chance that a “model F- value” so large could occur due to noise. ANOVA analysis also indicated that the model terms linear temperature (P < 0.0500), pH (P < 0.0500), substrate concentration (P < 0.0500), starch concentration (P < 0.0500), quadratic temperature A2 (P < 0. 0500), pH B2 (P < 0.0500), substrate concentration C2 (P < 0. 0500), starch concentration D2 (P < 0. 0500) and two interaction terms (AC, BC) were significant. Values of "Prob > F" less than 0.0500 indicate that the model terms are significant, while values greater than 0.1000 indicate that the model terms are not significant.
Table 3
ANOVA for response surface quadratic model Bacillus sp. NAB37
Source | Sum of Squares | df | Mean Square | F Value | p-value Prob > F |
Model | 32.04 | 14 | 2.29 | 172.41 | < 0.0001 |
A-Temp | 0.15 | 1 | 0.15 | 11.48 | 0.0041 |
B-pH | 0.20 | 1 | 0.20 | 14.81 | 0.0016 |
C-Substrate Conc | 9.99 | 1 | 9.99 | 752.98 | < 0.0001 |
D-Starch Conc | 0.25 | 1 | 0.25 | 18.57 | 0.0006 |
AB | 1.369E-003 | 1 | 1.369E-003 | 0.10 | 0.7525 |
AC | 0.36 | 1 | 0.36 | 27.39 | 0.0001 |
AD | 5.329E-003 | 1 | 5.329E-003 | 0.40 | 0.5359 |
BC | 0.10 | 1 | 0.10 | 7.62 | 0.0146 |
BD | 8.464E-003 | 1 | 8.464E-003 | 0.64 | 0.4370 |
CD | 9.604E-003 | 1 | 9.604E-003 | 0.72 | 0.4084 |
A2 | 10.05 | 1 | 10.05 | 757.17 | < 0.0001 |
B2 | 6.53 | 1 | 6.53 | 491.75 | < 0.0001 |
C2 | 0.25 | 1 | 0.25 | 19.01 | 0.0006 |
D2 | 7.46 | 1 | 7.46 | 562.15 | < 0.0001 |
Residual | 0.20 | 15 | 0.013 | | |
Lack of Fit | 0.16 | 10 | 0.016 | 2.16 | 0.2043 |
Pure Error | 0.037 | 5 | 7.480E-003 | | |
Cor Total | 32.24 | 29 | | | |
Std. Dev. | 0.12 | R-Squared | 0.9938 | |
Mean | 2.27 | Adj R-Squared | 0.9881 | |
C.V.% | 5.06 | Pred R-Squared | 0.9694 | |
Press | 0.99 | Adeq Precision | 52.229 | |
The 3D response surface plots were used to understand the effects of variables on CMCase production (Fig. 3). In each set, two variables varied within their experimental range, whereas the other two variables remained constant at zero level. The model predicted maximum CMCase production (5.16 U/ml) using 3% (w/v) substrate (pretreated Parthenium biomass), 1% (w/v) concentration of starch, at temperature 40oC and a of Ph 7.5. Figure 3(a) depicts the effect of interaction between pH and temperature on CMCase production by Bacillus sp. NAB37, when substrate and starch concentration were kept constant as 2% and 1% (w/v) respectively. The enzyme production increased with the increase in the initial pH upto the value of 7.5 at all temperatures, after which further rise in the pH resulted in a decline in the CMCase production. The highest enzyme synthesis was observed at temperature 40oC and pH 7.5. Figure 3(b) shows the interaction between temperature and the substrate concentration. When the pH value of 7.5 and starch levels of 1% were kept constant, the CMCase synthesis by the bacterial strain increased with the increase in the substrate concentration over entire temperature (35 to 45oC) range observed during the experiment. The activity, however, was maximum at temperature 40oC and substrate concentration of 3% (w/v). At 3% substrate levels, rise in the temperature beyond 40oC showed a gradual reduction in the production of the enzyme. Figure 3(c) represented the relationship between the starch concentration and temperature. The highest enzyme synthesis was observed at 40oC temperature and the starch concentration of 1% (w/v). The interaction between the substrate concentration and initial pH has been shown in Fig. 3(d). The surface plot revealed that higher substrate levels of 3% (w/v) were favorable for achieving high CMCase production at all pH levels, being maximum at pH 7.5. Figure 3(e) shows the effect of interaction between starch levels and pH, while keeping temperature as 40oC and substrate concentration 2%. The CMCase synthesis was maximum at pH 7.5 and starch concentration of 1%. Figure 3(f) indicated that high substrate levels induced high CMCase production. The maximum enzyme activity was recorded when substrate and starch concentration in the fermentation medium were 3% and 1% (w/v) respectively. The model was validated experimentally by carrying out CMCase production by Bacillus sp. NAB37 under conditions optimized by RSM. The experiments were performed in triplicates and the average CMCase production was seen. The maximum CMCase activity, 5.38U/ml was in good agreement with the value (5.16U/ml) predicted by the regression model. These results indicated that the developed model was accurate and reliable for predicting CMCase production by the Bacillus sp. NAB37.
The RSM technique has been used by various researchers to optimize cellulase production by different microorganisms and has also led to successful enhancement in the enzyme synthesis by knowing the interactions between influencing factors. The RSM study by Singh et al. [32] for the optimization of cellulase production from marine Bacillus VITRKHB has revealed maximum enzyme synthesis under optimized conditions of xylose 5.0%, beef extract 6.9%, NaCl 1.17%, pH 7.83 and temperature 25.84oC, after 24h of incubation. The statistical optimization of medium components for cellulase production by Enhydrobacter sp. ACCA2 using RSM method increased the CMCase synthesis up to 2.39-fold compared to that under unoptimized conditions when the CMC, peptone, (NH4)2SO4 and K2HPO4 were used at 15.00 g/l, 14.45 g/l, 0.45 g/l and 1.50 g/l concentrations [33].
Saccharification
In the case of the saccharification of pretreated P. hysterophorus biomass using bacterial (Bacillus sp. NAB37) cellulase, the highest hydrolysis yield was reached in 96h (Table 4, Fig. 4). Furthermore, the increase in the substrate concentration from 0.5–1% (w/v) resulted in an increase in the TRS from 0.167 ± 0.009 g/g biomass (≈ 26.83% saccharification yield) to 0.206 ± 0.009 g/g (≈ 33.11% saccharification yield). The amount of TRS obtained was 0.204 ± 0.012 g/g of the biomass when 2% substrate concentration as used (≈ 32.78% saccharification yield) (Table 4, Fig. 4). This value was insignificantly different from the value obtained when the substrate level was 1%. The saccharification process is considered good when it can hydrolyze higher loads of the biomass [34]. Therefore, the subsequent experiments were carried out using 2% (w/v) concentration of the substrate as the optimized level. The increase in the substrate levels from 2–7% resulted in a gradual decrease in the yield of TRS. Other studies have also documented that the increase in biomass concentration increases the viscosity of the system which interferes in the mass transfer of the enzymes and also the increased concentration of sugars tend to inhibit the enzyme [34, 35].
Table 4
Effect of substrate concentration on the TRS yield from hydrolysis of pretreated P. hysterophorus biomass using cellulase enzyme from Bacillus sp. NAB 37
Time (h) | Total reducing sugars (g/g biomass) at different substrate concentrations (%w/v) |
0.5 | 1.0 | 2.0 | 3.0 | 5.0 | 7.0 |
12 | 0.067 ± 0.011 | 0.078 ± 0.015 | 0.076 ± 0.014 | 0.069 ± 0.015 | 0.065 ± 0.013 | 0.062 ± 0.011 |
24 | 0.099 ± 0.009 | 0.111 ± 0.018 | 0.112 ± 0.009 | 0.097 ± 0.011 | 0.094 ± 0.018 | 0.089 ± 0.013 |
48 | 0.121 ± 0.014 | 0.145 ± 0.009 | 0.143 ± 0.016 | 0.131 ± 0.011 | 0.126.008 | 0.121 ± 0.016 |
72 | 0.144 ± 0.015 | 0.173 ± 0.010 | 0.170 ± 0.017 | 0.158 ± 0.012 | 0.153 ± 0.013 | 0.148 ± 0.007 |
96 | 0.167 ± 0.011 | 0.206 ± 0.009 | 0.204 ± 0.012 | 0.178 ± 0.012 | 0.171 ± 0.016 | 0.167 ± 0.013 |
● Hydrolysis conditions: 50°C temperature, pH 4.8, 120 rpm, enzyme loading: 30FPU per 100ml (or 0.3 FPU/ml) |
On studying the effect of bacterial cellulase enzyme loadings on the saccharification of the biomass, it was recorded that the amount of TRS released in the process increased significantly when the enzyme loading was increased from 5FPU to 30FPU in the reaction volume (100ml) and the hydrolysis time was 96h (Table 5). Maximum 0.204 ± 0.012g TRS per gram of the biomass was released (≈ 32.78% saccharification yield) in 96h when the enzyme was used at a concentration of 30FPU. Further rise in the enzyme loading to 40FPU resulted in an insignificant increase in the TRS, i.e., 0.208 ± 0.014g per gram of the biomass (Table 5, Fig. 5). Because a saccharification process involving use of the minimum amount of enzyme is most economical, therefore, 30FPU concentration of the enzyme was the optimized level in the current study. Furthermore, on studying the effect of hydrolysis time, it was found that the rate of hydrolysis increased almost linearly with the increase in the incubation time up to 96h (Fig. 5). The saccharification yield increased from 22.98% at 48h to 32.78% achieved in 96h. The stability of the enzyme, end product inhibition, and concentration of enzyme and substrate are among several factors influencing the rate of the saccharification process [36]. One of the probable reasons for the trend of hydrolysis rate in the present experiment could be the overall lower yield of sugars in the process.
Table 5
Effect of enzyme concentration on the TRS yield from hydrolysis of pretreated P. hysterophorus biomass using cellulase enzyme from Bacillus sp. NAB 37
Time (h) | Total reducing sugars (g/g biomass) at different enzyme loadings (FPU) |
5.0 | 10.0 | 20.0 | 30.0 | 40.0 | 50.0 |
12 | 0.019 ± 0.015 | 0.048 ± 0.013 | 0.066 ± 0.011 | 0.076 ± 0.014 | 0.079 ± 0.014 | 0.077 ± 0.014 |
24 | 0.029 ± 0.010 | 0.063 ± 0.011 | 0.086 ± 0.014 | 0.112 ± 0.009 | 0.111 ± 0.015 | 0.110 ± 0.015 |
48 | 0.041 ± 0.011 | 0.097 ± 0.012 | 0.121 ± 0.016 | 0.143 ± 0.016 | 0.146 ± 0.010 | 0.144 ± 0.010 |
72 | 0.055 ± 0.012 | 0.119 ± 0.011 | 0.157 ± 0.013 | 0.170 ± 0.017 | 0.176 ± 0.009 | 0.174 ± 0.009 |
96 | 0.073 ± 0.016 | 0.134 ± 0.011 | 0.175 ± 0.013 | 0.204 ± 0.012 | 0.208 ± 0.014 | 0.207 ± 0.012 |
● Hydrolysis conditions: 50°C temperature, pH 4.8, 120 rpm, 2% substrate (pretreated) concentration |
● The amount of the enzyme (in FPU per 100ml) was adjusted by adding corresponding volume of the enzyme in the reaction mixture |
Premalatha et al. [33] enhanced the cellulase production (8.86U/mL) from Enhydrobacter sp. ACCA2 by optimization of various parameters. When the same bacterial isolate was used for the saccharification of various biomass, it showed saccharification yield of > 40% in the sorghum leaves, sorghum stem and cumbu stem, > 50% in the cumbu leaves and the highest yield, i.e., > 60% in the bamboo. Alrumman [36] also optimized the cellulase production by Geobacillus stearothermophilus using alkali pretreated date palm waste and on using the same for optimization of the saccharification of alkali pretreated biomass observed pH 5.0, 50°C temperature, 4% biomass loading, 30FPU/g enzyme loading and hydrolysis time of 24h optimum for achieving saccharification yield of 71.03%. The yield, however, increased to 94.88% by the removal of the hydrolysate after 24h by using a two-step hydrolysis. Nargotra et al. [37] used the cellulase obtained from Bacillus subtilis SV1 (produced under optimized conditions) for the hydrolysis of ionic liquid pretreated pine needle biomass in a one pot consolidated bioprocess and was successful in obtaining the saccharification efficiency of 65.9%.