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Table 3 The time-course lactic acid production with Lactobacillus plantarum 23 and the consumption of glucose and xylose from hydrolysate of microalgal feedstock

From: Characterization of a heat-tolerant Chlorella sp. GD mutant with enhanced photosynthetic CO2 fixation efficiency and its implication as lactic acid fermentation feedstock

Time (h)

Control

WTa

M4b

Lactic acidc (g/L)

Glucose (g/L)

Glucose (g/L)

Xylose (g/L)

Glucose (g/L)

Xylose (g/L)

Control

WT

M4 mutant

0

20.5 ± 0.32

21.0 ± 0.33

1.9 ± 0.06

21.4 ± 0.29

2.1 ± 0.10

0

0

0

3

4.5 ± 0.17

2.65 ± 0.08

0.21 ± 0.00

2.75 ± 0.13

0.2 ± 0.01

11.60 ± 0.36

13.10 ± 0.54

13.45 ± 0.39

5

0

0

0

0

0

14.50 ± 0.28

16.10 ± 0.40

16.38 ± 0.62

8

0

0

0

0

0

14.40 ± 0.12

16.13 ± 0.08

16.45 ± 0.13

12

0

0

0

0

0

14.50 ± 0.12

16.13 ± 0.08

16.45 ± 0.13

24

0

0

0

0

0

14.50 ± 0.12

16.13 ± 0.08

16.45 ± 0.13

Conversion rated (%)

     

74.87

80.42

79.17

  1. The WT and M4 mutant feedstock was obtained after 8 days of culture under 6% CO2 condition. Pure glucose (used as control) in the fermentation broth of the control test was 20.5 g/L and accordingly, the content of glucose in the hydrolysate of the wild type (WT) and M4 mutant in the fermentation broth was adjusted to around 21 g/L with a xylose content of around 2 g/L. The conversion rate is estimated as (lactic acid content/theoretical lactic acid content) × 100 after 24 h of fermentation. The data are presented as mean ± SD (n = 3)
  2. a47.15 g day wt. of WT feedstock in 1 L fermentative mixture
  3. b39.28 g day wt. of M4 feedstock in 1 L fermentative mixture
  4. cLactic acid in 1 L fermentative mixture
  5. d(Real lactic acid content/theoretical lactic acid content) × 100