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Table 3 Results of fed-batch fermentation in biofilm reactors coupled with fixed-bed adsorption

From: Biobutanol production in a Clostridium acetobutylicum biofilm reactor integrated with simultaneous product recovery by adsorption

 

Fermentation with selective adsorption of butanol

Fermentation with co-adsorption of acetone

Fermentation with redox modulation

Fermentation time (h)

57

64

135

Glucose fermented (g/L)

198

297

367

Resin used (g)

418

812

910

Adsorbed ethanol (g)

1.8

0.82

2.2

Adsorbed acetone (g)

12.3

35.7

23.6

Adsorbed butanol (g)

42.1

68.1

84.7

Adsorbed acetoin (g)

0.40

2.4

1.2

Adsorbed butyrate (g)

1.9

3.1

8.7

Equivalent ethanol concentration (g/L)

5.1

4.8

6.8

Equivalent acetone concentration (g/L)

14.8

30.9

28.8

Equivalent butanol concentration (g/L)

38.2

58.3

92.6

Equivalent acetoin concentration (g/L)

1.7

2.6

2.6

Equivalent butyrate concentration (g/L)

1.7

2.4

10.8

aSolvent concentration (g/L)

59.8

96.5

130.7

aSolvent productivity (g · L-1 · h-1)

1.05

1.51

0.97

aSolvent yield (g/g)

0.302

0.325

0.356

bTotal product yield (g/g)

0.311

0.333

0.386

Butanol-acetone molar ratio

2.6c

1.9

3.2

  1. aSolvent: ABE and acetoin. bTotal product: ABE, acetoin, and butyrate. Acetate is not considered to be a product. cThe increased butanol-acetone ratio was probably due to the evaporation of acetone.