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Table 1 Performance of K. rhaeticus on fermentation media containing various mixing ratios of WDE with tap water, supplemented with different glycerol concentrations and the effect of media sterilization method on the fermentation efficiency

From: A sustainable bioprocess to produce bacterial cellulose (BC) using waste streams from wine distilleries and the biodiesel industry: evaluation of BC for adsorption of phenolic compounds, dyes and metals

WDE

Glycerol (g/L)

BC (g/L)

Productivity (g/L/d)

Carbon sources consumption (% w/w)

FAN consumption(% w/w)

WHC (w/w)1

WDE (% v/v)

Glucose

Fructose

Glycerol

Total

  

Thermal sterilization

 25

Crude, ≈20

3.7 ± 0.25f

0.42 ± 0.04e

70.0

6.3

91.5

87.9

71.8

86.2 ± 6.89b

 50

Crude, ≈20

5.1 ± 0.22e

0.56 ± 0.03d

72.0

5.0

93.4

83.8

78.4

84.3 ± 5.99c

 75

Crude, ≈20

6.6 ± 0.22d

0.67 ± 0.04c

82.0

25.0

92.9

81.7

72.2

89.5 ± 6.35a

 100

Crude, ≈20

8.1 ± 0.45c

0.81 ± 0.06b

82.4

14.7

98.9

85.5

83.1

82.6 ± 4.75d

 100

Crude, ≈30

9.0 ± 0.38b

0.90 ± 0.05a

58.3

33.3

95.2

81.5

84.3

60.1 ± 3.75f

 100

Crude, ≈45

4.0 ± 0.25f

0.45 ± 0.02e

31.4

10.0

65.1

57.6

76.2

87.1 ± 5.76b

 100

Pure, ≈30

9.8 ± 0.42a

0.98 ± 0.06a

47.3

35.8

84.5

72.6

87.3

56.6 ± 4.01 g

 0

Crude, ≈30

5.1 ± 0.29e

0.46 ± 0.03e

–

–

57.6

57.6

52.1

68.4 ± 4.99e

Filter sterilization

 100

Crude, ≈30

6.6 ± 0.15d

0.66 ± 0.02c

100

17.2

60.4

57.4

72.7

86.0 ± 8.69b

  1. 1 g water/g dry BC; Different superscript letters within same individual columns indicate statistically significant differences (p < 0.05)