Skip to main content

Table 1 Operating conditions of the bioreactor

From: Upgrading dilute ethanol to odd-chain carboxylic acids by a synthetic co-culture of Anaerotignum neopropionicum and Clostridium kluyveri

Phase

Period (days)

ELR

(g L−1 d−1) [mM d−1]

HRT

(h)

Ethanol inflow (mM)

Remark

Batch

0

–

2.1

–

–

–

–

A

2.1

–

3

1.7 [35]

36

51

Start of the continuous operation

B

3

–

17.8

1.7 [35]

36

51

Gas flowrate increased to 0.07 vvm

C

17.8

–

29.7

3.1 [64]

36

95

–

D

29.7

–

32.9

8.0 [171]

42

300

–

E.1

32.9

–

43.7

6.3 [122]

54

300

–

E.2

43.7

–

100.7

6.3 [122]

54

300

Technical issuesa

F

100.7

–

155.7

6.7 [145]

54

319

Technical issues fixed and new medium tank

G

155.7

–

160

6.7 [145]

54

320

pH increased to 7.3

  1. ELR ethanol loading rate
  2. HRT hydraulic retention time
  3. aThe outflow line clogged on day 55. In addition, during this period ethanol was slowly being stripped out of the medium tank