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Table 3 Overview of critical performance parameters for the bioreactor with pertraction (BP; pH 6) and the bioreactor without pertraction (BNP; pH 7) for the different operating phases as defined in Table 1 (average ± stdev)

From: Upgrading syngas fermentation effluent using Clostridium kluyveri in a continuous fermentation

 

Phase

OLR (g COD L−1 day−1)

OLR (mM-C day−1)

n-Butyric acid (mM day−1)

n-Caproic acid  (mM day−1)

n-Caprylic acid (mM day−1)

Specificity C6 (%)

Specificity C8 (%)

Carbon conversion efficiency  (%)

Extr. C6 (%)

Extr. C8 (%)

BP

II–III

7.0 ± 0.4

151.9 ± 31.4

0.9 ± 0.7

8.4 ± 8.4

0.2 ± 0.1

88.5 ± 10.1

3.7 ± 2.9

38.9 ± 17.4

80.4 ± 10.5

100.0 ± 0.0

IV

10.9 ± 0.4

255.2 ± 7.4

1.3 ± 0.2

16.2 ± 5.4

0.6 ± 0.4

90.9 ± 2.0

3.9 ± 2.2

41.9 ± 2.5

64.8 ± 13.7

94.4 ± 6.6

 V

14.2 ± 1.0

298.3 ± 9.6

1.7 ± 0.4

19.1 ± 6.6

1.0 ± 0.4

87.7 ± 3.9

6.4 ± 3.0

38.5 ± 12.6

37.8 ± 27.2

65.0 ± 26.5

 VI

16.3 ± 0.4

370.0 ± 9.7

9.4 ± 0.7

39.9 ± 0.9

1.4 ± 0.2

83.0 ± 1.0

4.0 ± 0.4

79.9 ± 2.0

42.7 ± 6.9

77.0 ± 4.5

 VII

10.7 ± 3.3

244.6 ± 74.4

7.8 ± 0.11

23.1 ± 4.7

0.47 ± 0.3

79.5 ± 1.9

1.9 ± 1.6

76.4 ± 19.5

70.0 ± 40

101 ± 2.7

BNP

 II

6.9 ± 0.2

122.5 ± 31.7

1.0 ± 0.3

11.1 ± 2.7

0.8 ± 0.2

86.5 ± 0.5

8.1 ± 0.2

65.9 ± 17.4

  

 III–IV

10.9 ± 0.4

233.0 ± 7.9

1.7 ± 0.3

15.7 ± 0.5

1.2 ± 0.1

85.5 ± 1.2

8.5 ± 0.4

47.5 ± 2.5

  

 V

11.3 ± 1.2

241.0 ± 28.4

1.5 ± 0.2

18.6 ± 2.9

1.8 ± 0.3

84.7 ± 1.5

10.8 ± 1.2

54.7 ± 6.5

  

 VI

13.0 ± 0.03

296.5 ± 0.7

7.8 ± 0.7

37.6 ± 1.6

2.6 ± 0.01

81.4 ± 0.5

7.4 ± 0.3

93.6 ± 4.4

  

 VII

12.3 ± 1.2

279.7 ± 27

5.7 ± 0.7

35.3 ± 2.7

2.14 ± 0.4

84.2 ± 1.0

6.7 ± 0.7

90.1 ± 0.7

  
  1. COD chemical oxygen demand, C6 n-caproic acid, C8 n-caprylic acid, Extr. extraction efficiency
  2. Production rates for the three products (n-butyric, n-caproic and n-caprylic acid) are shown. Weighted averages were taken for the steady state periods (starting 3 HRTs after a change in condition), and for n ≥ 3