Skip to main content
. 2019 Feb 7;18:30. doi: 10.1186/s12934-019-1084-2

Fig. 8.

Fig. 8

Typical kinetics of isobutanol production by strain YHS6 (mutant 10 harboring plasmid pSA69) in a 3-L bioreactor at 30 °C. For a, total isobutanol production which was calculated as sum of isobutanol in collection bottles A, B, C and the broth with a working volume of 2 L, and the isobutanol production in broth. For b, cell growth and glucose consumption during the whole fermentation process