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Figure 8

Figure 8. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Fermentation profile of fed-batch enzymatic hydrolysate.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
3.
Figure 3

Figure 3. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Plot between the experimental versus predicted insoluble solids during the fed-batch enzymatic hydrolysis.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
4.
Figure 4

Figure 4. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Comparative profiling of batch and fed-batch enzymatic saccharification (A) glucose production, (B) cellulose conversion.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
5.
Figure 1

Figure 1. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Plot between substrate concentrations versus time for the enzymatic saccharification of delignified lignocellulosic biomass at different initial substrate consistencies.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
6.
Figure 6

Figure 6. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Kinetic simulation profile for the volume of bioreactor at different initial substrate consistency (5-15%) using dilution rate of (A) 0.1 h-1, (B) 0.2 h-1, (C) 0.3 h-1 and (D) 0.4 h-1.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
7.
Figure 5

Figure 5. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Kinetic simulation profile for cumulative insoluble solids feeding at different initial substrate concentration (5-15%) at varied dilution rate of (A) 0.1 h-1, (B) 0.2 h-1, (C) 0.3 h-1 and (D) 0.4 h-1.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.
8.
Figure 2

Figure 2. From: Kinetic study of batch and fed-batch enzymatic saccharification of pretreated substrate and subsequent fermentation to ethanol.

Plots between the actual and the predicted values of glucose concentration released during the enzymatic hydrolysis of delignified lignocellulosic biomass at 5% (A), 10% (B), 15% (C) and 20% (D) initial substrate consistencies.

Rishi Gupta, et al. Biotechnol Biofuels. 2012;5:16-16.

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