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Table 3 Isopropanol–butanol (IB) fermentation with various ratios of glucose and glycerol

From: Effective isopropanol–butanol (IB) fermentation with high butanol content using a newly isolated Clostridium sp. A1424

 

Ratio of glucose:glycerol (g:g)

22:0

20:2

18:4

14:8c

9:13c

Substrate consumption

 Glucose (g/L) [mM]

21.85±0.27

[121.25]

19.85±0.45

[110.16]

17.62±0.69

[97.78]

13.35±0.31

[74.10]

8.98±0.20

[49.82]

 Glycerol (g/L) [mM]

0

[0]

1.83±0.61

[19.82]

3.59±0.30

[38.97]

7.01±0.14

[76.08]

10.94±3.25

[118.79]

 Total carbon (mM)

727.53

720.43

703.59

672.83

655.27

 NAD(P)H from glycolysis (mM)

242.51

259.97

273.50

300.36

337.21

 NAD(P)HC (mol/mol)d

0.33

0.36

0.39

0.45

0.51

Metabolite production

 Butanol (g/L)

4.33±0.00

4.66±0.03

5.04±0.08

5.38±0.01

5.09±0.09

 Isopropanol (g/L)

2.44±0.05

2.24±0.03

2.07±0.04

1.57±0.02

0.83±0.03

 Acetone (g/L)

0.28±0.00

0.18±0.01

0

0

0

 Butyric acid (g/L)

0.69±0.02

0.73±0.12

0.59±0.00

0.98±0.04

1.95±0.03

 Acetic acid (g/L)

0.51±0.00

0.46±0.00

0.43±0.00

0.24±0.02

0.11±0.02

 NAD(P)H requirement for product (mM)

290.02

305.35

319.82

338.44

332.62

 Ratio of B/Ia (g/g)

1.78

2.07

2.43

3.43

6.14

 Y bB (g/g)

0.20

0.21

0.24

0.26

0.26

 Y bIB (g/g)

0.31

0.32

0.34

0.34

0.30

  1. The values are average and one standard deviation of triplicate experiments
  2. The fermentation was performed on serum bottle without pH control
  3. The data were obtained at 28 h of fermentation except 9:13 (25 h)
  4. aB/I butanol concentration divided by isopropanol concentration
  5. b Y B, butanol yield (g butanol/g substrate); Y IB, the sum of butanol and isopropanol yield (g [butanol + isopropanol]/g substrate)
  6. cAfter fermentations, 0.39 and 2.48 g/L glycerol remained on the ratio of 14:8 and 9:13, respectively
  7. dNAD(P)HC: The generation of NAD(P)H mole per consumed substrate carbon mole