Figures & data
Table 1. Growth models considered for the data evaluation.[Citation30–32]
Table 2. Estimated kinetic parameters by hybrid GA/PSO method and value of objective function for various kinetic models.
Figure 4. Comparison of the experimental and simulated data of batch fermentation by various growth kinetic models: Aiba (a), Andrews (b), Contois (c), Haldane (d), Monod (e), Moser (f), and Tessier (g). Experimental concentrations of X (٭), S (○), and P (◊) vs. hybrid GA/PSO simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L.
![Figure 4. Comparison of the experimental and simulated data of batch fermentation by various growth kinetic models: Aiba (a), Andrews (b), Contois (c), Haldane (d), Monod (e), Moser (f), and Tessier (g). Experimental concentrations of X (٭), S (○), and P (◊) vs. hybrid GA/PSO simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L.](/cms/asset/c9a3888a-2fd9-4e4e-9a40-2b896f98ab3d/tbeq_a_1077686_f0004_b.gif)
Figure 5. Comparison of the experimental and simulated data of fed-batch fermentation by various growth kinetic models: Aiba (a), Andrews (b), Contois (c), Haldane (d), Monod (e), Moser (f), and Tessier (g). Experimental concentrations of X (٭), S (○), and P (◊) vs. hybrid GA/PSO simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L; feed rate = 0.01 L/h.
![Figure 5. Comparison of the experimental and simulated data of fed-batch fermentation by various growth kinetic models: Aiba (a), Andrews (b), Contois (c), Haldane (d), Monod (e), Moser (f), and Tessier (g). Experimental concentrations of X (٭), S (○), and P (◊) vs. hybrid GA/PSO simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L; feed rate = 0.01 L/h.](/cms/asset/9e484aaa-92c1-4327-be4c-8c58b8812a4a/tbeq_a_1077686_f0005_b.gif)
Figure 6. Comparison of the experimental and simulated data of batch fermentation by the Contois model by using GA (a) and PSO (b). Experimental concentrations of X (٭), S (○), and P (◊) vs. simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L.
![Figure 6. Comparison of the experimental and simulated data of batch fermentation by the Contois model by using GA (a) and PSO (b). Experimental concentrations of X (٭), S (○), and P (◊) vs. simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L.](/cms/asset/be73833a-bebb-4e9a-8810-89b54d7ffcc8/tbeq_a_1077686_f0006_b.gif)
Figure 7. Comparison of the experimental and simulated data of fed-batch fermentation by the Contois model by using GA (a) and PSO (b). Experimental concentrations of X (٭), S (○), and P (◊) vs. simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L; feed rate = 0.01 L/h.
![Figure 7. Comparison of the experimental and simulated data of fed-batch fermentation by the Contois model by using GA (a) and PSO (b). Experimental concentrations of X (٭), S (○), and P (◊) vs. simulated data (solid lines). Note: X, biomass (B. licheniformis); S, substrate (glucose); P, product (protease). Initial concentration of substrate is 40 g/L; feed rate = 0.01 L/h.](/cms/asset/974bfe3a-f48b-4075-81e9-34c162cc81d5/tbeq_a_1077686_f0007_b.gif)
Table 3. Comparison of performance across GA, PSO, and hybrid GA/PSO.