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Table 2 Butanol production with C. pasteurianum CH4 through batch fermentation using non-VMD-integrated and VMD-integrated processes with and without butyrate addition

From: Bio-butanol production from glycerol with Clostridium pasteurianum CH4: the effects of butyrate addition and in situ butanol removal via membrane distillation

Fermentation conditions

Butanol concentration (g L−1)

Glycerol conversion (%)

Average butanol production rate (g L−1 h−1)

Butanol yield (mol butanol/mol glycerol)

Non-VMD-integrated fermentation

Without butyrate addition

12.6 ± 0.8

63.4 ± 2.1

0.12 ± 0.02

0.24 ± 0.01

With butyrate addition

12.1 ± 0.6

46.4 ± 0.5

0.14 ± 0.01

0.34 ± 0.04

VMD-integrated fermentation

Without butyrate addition

17.1 ± 0.3

96.5 ± 1.8

0.16 ± 0.02

0.23 ± 0.02

With butyrate addition

29.8 ± 1.2

96.8 ± 0.9

0.29 ± 0.05

0.39 ± 0.01