Multiphase Bioreactor Design

(avery) #1
0.042 0.07 0.06
0.050 0.09 0.12
0.058 0.20 0.24
0.025 0.02 0.01
0.033 0.02 0.02
0.042 0.02 0.02

0.017


0.050 0.03 0.04
0.025 0 0
0.033 0 0
0.042 0 0

0.029


0.050 0 0

b) Kaštánek, Zahradník, Rylek (1974): Dr=0.292 m, N=3, dn=1.6 mm


uoL
m/s


103 uoG
m/s

E
φ=4%

v
φ=8%
0.008 1.35 1.79
0.025 2.05 2.40

2.5


0.042 3.04 2.93
0.008 0.12 0.29
0.025 0.27 0.45

7.5


0.042 0.53 0.76

Table 1.3 Comparison of characteristic coordinates


of experimental and calculated RTD curves


(^) Number of stages column
uoL N=3 N=6
m/s
uoG
m/s
θ
exp
Ymax
calc


Y

exp

θ=1
calc

Eav θ
exp

Ymax
calc

Y

exp

θ=1
calc

Eav

0.025 0.60 0.57 0.62 0.60 0.34 0.73 0.70 0.80 0.79 0.28
0.033 0.54 0.52 0.55 0.54 0.52 0.69 0.65 0.77 0.74 0.49
0.042 0.48 0.47 0.53 0.52 0.75 0.67 0.63 0.72 0.71 0.61
0.050 0.46 0.44 0.51 0.49 1.09 0.63 0.62 0.65 0.63 1.14

0.004


0.058 0.38 0.36 0.48 0.48 1.93 0.53 0.51 0.57 0.55 1.89

0.017 0.025 0.69 0.68 0.71 0.70 0.02 0.84 0.84 0.99 0.99 0.01


0.033 0.68 0.68 0.70 0.70 0.02 0.84 0.83 1.01 0.98 0.02

Multiphase bioreactor design 8  
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