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. 2011 Jul;77(13):4473–4485. doi: 10.1128/AEM.00116-11

Table 7.

Results for C. beijerinckii SA-1/ATCC 35702 cultivated in a two-stage, one-feed-stream chemostat culture containing d-glucose and d-xylose in the validated mediuma

Reactor Overall D (h−1) pH Mean concn (g/liter) ± SD of the following fermentation product:
Proportion (%) of sugar that was consumed
Butanol yield (mol/mol of substrate) No. of vegetative cells No. of spores
Acetate Butyrate Acetone Butanol d-Glucose d-Xylose
First reactor 0.102 6.5 3.3 ± 0.6 6.3 ± 0.5 0.2 ± 0.1 0.5 ± 0.3 69.2 31.0
Second reactor 0.04 6.5 1.6 ± 0.8 6.4 ± 3.0 0.2 ± 0.1 0.4 ± 0.2 93.3 59.1 0.018 7.3 E7 2.3 E8
0.05 6.5 1.2 ± 1.0 4.0 ± 0.8 0.5 ± 0.2 1.8 ± 0.8 96.9 67.6 0.078 1.4 E8 1.5 E8
0.06 6.5 2.0 ± 1.0 1.6 ± 1.0 5.3 ± 0.6 7.2 ± 0.2 83.2 52.9 0.380 1.8 E8 1.3 E8
0.04 Free 2.7 ± 0.2 3.2 ± 1.2 1.1 ± 0.1 3.7 ± 0.4 95.7 47.5 0.183
0.05 Free 2.0 ± 0.4 3.5 ± 0.2 0.5 ± 0.1 2.0 ± 0.1 96.6 32.7 0.105
0.06 Free 2.0 ± 0.1 3.2 ± 0.9 0.4 ± 0.1 2.1 ± 0.5 93.5 57.6 0.100
a

C. beijerinckii SA-1/ATCC 35702 was cultivated in a two-stage, one-feed-stream chemostat culture containing d-glucose (40 g/liter) and d-xylose (20 g/liter) in the validated medium described in Table 4 at 37°C and pH 6.5. The dilution rate (D) and pH were varied in the second reactor.