Mol Syst Biol. 2011 Mar;7:477. Large-scale 13C-flux analysis reveals distinct transcriptional control of respiratory and fermentative metabolism in Escherichia coli. Haverkorn van Rijsewijk BR, Nanchen A, Nallet S, et al.
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| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| ATP production rate Maximum | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R00267+2.5*R08549-R00405+1.5*R00402+2.5*R00342 +2.5*R00214 |
| ATP production rate Minium | N/A | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | N/A | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | N/A | R02736+R01528 |
| Growth Condition | |
| Strains | Escherichia coli BW25113 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 wild type |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.6/h |
| Case-specific description | wild type |
| Growth Condition | |
| Strains | Escherichia coli BW25114 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AlsR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | AlsR |
| Growth Condition | |
| Strains | Escherichia coli BW25115 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AppY |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | AppY |
| Growth Condition | |
| Strains | Escherichia coli BW25116 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArcA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | ArcA |
| Growth Condition | |
| Strains | Escherichia coli BW25117 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArcB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | ArcB |
| Growth Condition | |
| Strains | Escherichia coli BW25118 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArgR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.46/h |
| Case-specific description | ArgR |
| Growth Condition | |
| Strains | Escherichia coli BW25119 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AscG |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | AscG |
| Growth Condition | |
| Strains | Escherichia coli BW25120 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 BasR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | BasR |
| Growth Condition | |
| Strains | Escherichia coli BW25121 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 BolA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | BolA |
| Growth Condition | |
| Strains | Escherichia coli BW25122 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ChpB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | ChpB |
| Growth Condition | |
| Strains | Escherichia coli BW25123 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CpxR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | CpxR |
| Growth Condition | |
| Strains | Escherichia coli BW25124 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Cra |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | Cra |
| Growth Condition | |
| Strains | Escherichia coli BW25125 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CreB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | CreB |
| Growth Condition | |
| Strains | Escherichia coli BW25126 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Crl |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.46/h |
| Case-specific description | Crl |
| Growth Condition | |
| Strains | Escherichia coli BW25127 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Crp |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.32/h |
| Case-specific description | Crp |
| Growth Condition | |
| Strains | Escherichia coli BW25128 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CsgD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | CsgD |
| Growth Condition | |
| Strains | Escherichia coli BW25129 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | CspA |
| Growth Condition | |
| Strains | Escherichia coli BW25130 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CysB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.47/h |
| Case-specific description | CysB |
| Growth Condition | |
| Strains | Escherichia coli BW25131 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CytR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | CytR |
| Growth Condition | |
| Strains | Escherichia coli BW25132 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 DcuR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.57/h |
| Case-specific description | DcuR |
| Growth Condition | |
| Strains | Escherichia coli BW25133 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 EvgA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.59/h |
| Case-specific description | EvgA |
| Growth Condition | |
| Strains | Escherichia coli BW25134 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FadR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | FadR |
| Growth Condition | |
| Strains | Escherichia coli BW25135 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FhlA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.58/h |
| Case-specific description | FhlA |
| Growth Condition | |
| Strains | Escherichia coli BW25136 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fis |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.66/h |
| Case-specific description | Fis |
| Growth Condition | |
| Strains | Escherichia coli BW25137 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FlhD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | FlhD |
| Growth Condition | |
| Strains | Escherichia coli BW25138 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FliZ |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | FliZ |
| Growth Condition | |
| Strains | Escherichia coli BW25139 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fnr |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | Fnr |
| Growth Condition | |
| Strains | Escherichia coli BW25140 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FrvR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | FrvR |
| Growth Condition | |
| Strains | Escherichia coli BW25141 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fur |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.47/h |
| Case-specific description | Fur |
| Growth Condition | |
| Strains | Escherichia coli BW25142 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadE |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | GadE |
| Growth Condition | |
| Strains | Escherichia coli BW25143 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadW |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | GadW |
| Growth Condition | |
| Strains | Escherichia coli BW25144 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadX |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | GadX |
| Growth Condition | |
| Strains | Escherichia coli BW25145 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GcvA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | GcvA |
| Growth Condition | |
| Strains | Escherichia coli BW25146 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GlcC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | GlcC |
| Growth Condition | |
| Strains | Escherichia coli BW25147 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GlpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.4/h |
| Case-specific description | GlpR |
| Growth Condition | |
| Strains | Escherichia coli BW25148 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 HdfR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.49/h |
| Case-specific description | HdfR |
| Growth Condition | |
| Strains | Escherichia coli BW25149 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Hns |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.44/h |
| Case-specific description | Hns |
| Growth Condition | |
| Strains | Escherichia coli BW25150 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IclR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | IclR |
| Growth Condition | |
| Strains | Escherichia coli BW25151 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IdnR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | IdnR |
| Growth Condition | |
| Strains | Escherichia coli BW25152 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IHF A |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.44/h |
| Case-specific description | IHF A |
| Growth Condition | |
| Strains | Escherichia coli BW25153 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IHF B |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | IHF B |
| Growth Condition | |
| Strains | Escherichia coli BW25154 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 KdgR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | KdgR |
| Growth Condition | |
| Strains | Escherichia coli BW25155 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 LldR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.57/h |
| Case-specific description | LldR |
| Growth Condition | |
| Strains | Escherichia coli BW25156 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 LrhA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.49/h |
| Case-specific description | LrhA |
| Growth Condition | |
| Strains | Escherichia coli BW25157 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Lrp |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.45/h |
| Case-specific description | Lrp |
| Growth Condition | |
| Strains | Escherichia coli BW25158 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 MarA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | MarA |
| Growth Condition | |
| Strains | Escherichia coli BW25159 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 MarR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | MarR |
| Growth Condition | |
| Strains | Escherichia coli BW25160 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Mlc |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | Mlc |
| Growth Condition | |
| Strains | Escherichia coli BW25161 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ModE |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | ModE |
| Growth Condition | |
| Strains | Escherichia coli BW25162 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NagC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | NagC |
| Growth Condition | |
| Strains | Escherichia coli BW25163 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NarL |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | NarL |
| Growth Condition | |
| Strains | Escherichia coli BW25164 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NarP |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | NarP |
| Growth Condition | |
| Strains | Escherichia coli BW25165 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NsrR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | NsrR |
| Growth Condition | |
| Strains | Escherichia coli BW25166 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NtrC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.57/h |
| Case-specific description | NtrC |
| Growth Condition | |
| Strains | Escherichia coli BW25167 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OgrK |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.49/h |
| Case-specific description | OgrK |
| Growth Condition | |
| Strains | Escherichia coli BW25168 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OmpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | OmpR |
| Growth Condition | |
| Strains | Escherichia coli BW25169 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OxyR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | OxyR |
| Growth Condition | |
| Strains | Escherichia coli BW25170 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PdhR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | PdhR |
| Growth Condition | |
| Strains | Escherichia coli BW25171 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PerR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | PerR |
| Growth Condition | |
| Strains | Escherichia coli BW25172 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PhoB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | PhoB |
| Growth Condition | |
| Strains | Escherichia coli BW25173 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PrpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | PrpR |
| Growth Condition | |
| Strains | Escherichia coli BW25174 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PspC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | PspC |
| Growth Condition | |
| Strains | Escherichia coli BW25175 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PurR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | PurR |
| Growth Condition | |
| Strains | Escherichia coli BW25176 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 QseB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | QseB |
| Growth Condition | |
| Strains | Escherichia coli BW25177 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RcsA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.59/h |
| Case-specific description | RcsA |
| Growth Condition | |
| Strains | Escherichia coli BW25178 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RcsB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | RcsB |
| Growth Condition | |
| Strains | Escherichia coli BW25179 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Rob |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | Rob |
| Growth Condition | |
| Strains | Escherichia coli BW25180 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RutR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | RutR |
| Growth Condition | |
| Strains | Escherichia coli BW25181 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SdiA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | SdiA |
| Growth Condition | |
| Strains | Escherichia coli BW25182 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SoxR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | SoxR |
| Growth Condition | |
| Strains | Escherichia coli BW25183 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SoxS |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | SoxS |
| Growth Condition | |
| Strains | Escherichia coli BW25184 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | SspA |
| Growth Condition | |
| Strains | Escherichia coli BW25185 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TdcA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | TdcA |
| Growth Condition | |
| Strains | Escherichia coli BW25186 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TdcR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | TdcR |
| Growth Condition | |
| Strains | Escherichia coli BW25187 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TorR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.58/h |
| Case-specific description | TorR |
| Growth Condition | |
| Strains | Escherichia coli BW25188 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | UspA |
| Growth Condition | |
| Strains | Escherichia coli BW25189 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UvrY |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.48/h |
| Case-specific description | UvrY |
| Growth Condition | |
| Strains | Escherichia coli BW25190 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UxuR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | UxuR |
| Growth Condition | |
| Strains | Escherichia coli BW25191 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YbhD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | YbhD |
| Growth Condition | |
| Strains | Escherichia coli BW25192 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YdeO |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | YdeO |
| Growth Condition | |
| Strains | Escherichia coli BW25193 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YdjF |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | YdjF |
| Growth Condition | |
| Strains | Escherichia coli BW25194 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YfhA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.55/h |
| Case-specific description | YfhA |
| Growth Condition | |
| Strains | Escherichia coli BW25195 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ElbB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | ElbB |
| Growth Condition | |
| Strains | Escherichia coli BW25196 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FecI |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | FecI |
| Growth Condition | |
| Strains | Escherichia coli BW25197 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FlgM |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.5/h |
| Case-specific description | FlgM |
| Growth Condition | |
| Strains | Escherichia coli BW25198 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FliA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | FliA |
| Growth Condition | |
| Strains | Escherichia coli BW25199 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.51/h |
| Case-specific description | RpoD |
| Growth Condition | |
| Strains | Escherichia coli BW25200 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoN |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.35/h |
| Case-specific description | RpoN |
| Growth Condition | |
| Strains | Escherichia coli BW25201 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoS |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.56/h |
| Case-specific description | RpoS |
| Growth Condition | |
| Strains | Escherichia coli BW25202 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Rsd |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.52/h |
| Case-specific description | Rsd |
| Growth Condition | |
| Strains | Escherichia coli BW25203 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RseA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | RseA |
| Growth Condition | |
| Strains | Escherichia coli BW25204 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RseB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.54/h |
| Case-specific description | RseB |
| Growth Condition | |
| Strains | Escherichia coli BW25205 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Pgi |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.32/h |
| Case-specific description | Pgi |
| Growth Condition | |
| Strains | Escherichia coli BW25206 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Zwf |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.44/h |
| Case-specific description | Zwf |
| Growth Condition | |
| Strains | Escherichia coli BW25207 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SdhC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glucose |
| Growth rate | 0.53/h |
| Case-specific description | SdhC |
| Growth Condition | |
| Strains | Escherichia coli BW25208 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 wild type |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | wild type |
| Growth Condition | |
| Strains | Escherichia coli BW25209 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AlsR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | AlsR |
| Growth Condition | |
| Strains | Escherichia coli BW25210 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AppY |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | AppY |
| Growth Condition | |
| Strains | Escherichia coli BW25211 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArcA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | ArcA |
| Growth Condition | |
| Strains | Escherichia coli BW25212 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArcB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | ArcB |
| Growth Condition | |
| Strains | Escherichia coli BW25213 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ArgR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | ArgR |
| Growth Condition | |
| Strains | Escherichia coli BW25214 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 AscG |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | AscG |
| Growth Condition | |
| Strains | Escherichia coli BW25215 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 BasR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.2/h |
| Case-specific description | BasR |
| Growth Condition | |
| Strains | Escherichia coli BW25216 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 BolA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | BolA |
| Growth Condition | |
| Strains | Escherichia coli BW25217 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ChpB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | ChpB |
| Growth Condition | |
| Strains | Escherichia coli BW25218 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CpxR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.16/h |
| Case-specific description | CpxR |
| Growth Condition | |
| Strains | Escherichia coli BW25219 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Cra |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.34/h |
| Case-specific description | Cra |
| Growth Condition | |
| Strains | Escherichia coli BW25220 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CreB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | CreB |
| Growth Condition | |
| Strains | Escherichia coli BW25221 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Crl |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | Crl |
| Growth Condition | |
| Strains | Escherichia coli BW25222 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Crp |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.09/h |
| Case-specific description | Crp |
| Growth Condition | |
| Strains | Escherichia coli BW25223 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CsgD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | CsgD |
| Growth Condition | |
| Strains | Escherichia coli BW25224 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.22/h |
| Case-specific description | CspA |
| Growth Condition | |
| Strains | Escherichia coli BW25225 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CysB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | CysB |
| Growth Condition | |
| Strains | Escherichia coli BW25226 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 CytR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | CytR |
| Growth Condition | |
| Strains | Escherichia coli BW25227 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 DcuR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | DcuR |
| Growth Condition | |
| Strains | Escherichia coli BW25228 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 EvgA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | EvgA |
| Growth Condition | |
| Strains | Escherichia coli BW25229 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FadR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | FadR |
| Growth Condition | |
| Strains | Escherichia coli BW25230 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FhlA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | FhlA |
| Growth Condition | |
| Strains | Escherichia coli BW25231 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fis |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.24/h |
| Case-specific description | Fis |
| Growth Condition | |
| Strains | Escherichia coli BW25232 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FlhD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | FlhD |
| Growth Condition | |
| Strains | Escherichia coli BW25233 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FliZ |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | FliZ |
| Growth Condition | |
| Strains | Escherichia coli BW25234 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fnr |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | Fnr |
| Growth Condition | |
| Strains | Escherichia coli BW25235 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FrvR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | FrvR |
| Growth Condition | |
| Strains | Escherichia coli BW25236 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Fur |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | Fur |
| Growth Condition | |
| Strains | Escherichia coli BW25237 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadE |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | GadE |
| Growth Condition | |
| Strains | Escherichia coli BW25238 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadW |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | GadW |
| Growth Condition | |
| Strains | Escherichia coli BW25239 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GadX |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | GadX |
| Growth Condition | |
| Strains | Escherichia coli BW25240 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GcvA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | GcvA |
| Growth Condition | |
| Strains | Escherichia coli BW25241 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GlcC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | GlcC |
| Growth Condition | |
| Strains | Escherichia coli BW25242 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 GlpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.14/h |
| Case-specific description | GlpR |
| Growth Condition | |
| Strains | Escherichia coli BW25243 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 HdfR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.2/h |
| Case-specific description | HdfR |
| Growth Condition | |
| Strains | Escherichia coli BW25244 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Hns |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.12/h |
| Case-specific description | Hns |
| Growth Condition | |
| Strains | Escherichia coli BW25245 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IclR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | IclR |
| Growth Condition | |
| Strains | Escherichia coli BW25246 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IdnR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | IdnR |
| Growth Condition | |
| Strains | Escherichia coli BW25247 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IHF A |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.4/h |
| Case-specific description | IHF A |
| Growth Condition | |
| Strains | Escherichia coli BW25248 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 IHF B |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.45/h |
| Case-specific description | IHF B |
| Growth Condition | |
| Strains | Escherichia coli BW25249 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 KdgR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | KdgR |
| Growth Condition | |
| Strains | Escherichia coli BW25250 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 LldR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | LldR |
| Growth Condition | |
| Strains | Escherichia coli BW25251 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 LrhA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | LrhA |
| Growth Condition | |
| Strains | Escherichia coli BW25252 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Lrp |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.14/h |
| Case-specific description | Lrp |
| Growth Condition | |
| Strains | Escherichia coli BW25253 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 MarA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | MarA |
| Growth Condition | |
| Strains | Escherichia coli BW25254 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 MarR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | MarR |
| Growth Condition | |
| Strains | Escherichia coli BW25255 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Mlc |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.27/h |
| Case-specific description | Mlc |
| Growth Condition | |
| Strains | Escherichia coli BW25256 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ModE |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | ModE |
| Growth Condition | |
| Strains | Escherichia coli BW25257 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NagC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.46/h |
| Case-specific description | NagC |
| Growth Condition | |
| Strains | Escherichia coli BW25258 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NarL |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | NarL |
| Growth Condition | |
| Strains | Escherichia coli BW25259 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NarP |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | NarP |
| Growth Condition | |
| Strains | Escherichia coli BW25260 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NsrR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | NsrR |
| Growth Condition | |
| Strains | Escherichia coli BW25261 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 NtrC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.2/h |
| Case-specific description | NtrC |
| Growth Condition | |
| Strains | Escherichia coli BW25262 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OgrK |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | OgrK |
| Growth Condition | |
| Strains | Escherichia coli BW25263 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OmpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | OmpR |
| Growth Condition | |
| Strains | Escherichia coli BW25264 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 OxyR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | OxyR |
| Growth Condition | |
| Strains | Escherichia coli BW25265 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PdhR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | PdhR |
| Growth Condition | |
| Strains | Escherichia coli BW25266 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PerR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | PerR |
| Growth Condition | |
| Strains | Escherichia coli BW25267 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PhoB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | PhoB |
| Growth Condition | |
| Strains | Escherichia coli BW25268 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PrpR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | PrpR |
| Growth Condition | |
| Strains | Escherichia coli BW25269 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PspC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | PspC |
| Growth Condition | |
| Strains | Escherichia coli BW25270 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 PurR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | PurR |
| Growth Condition | |
| Strains | Escherichia coli BW25271 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 QseB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | QseB |
| Growth Condition | |
| Strains | Escherichia coli BW25272 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RcsA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | RcsA |
| Growth Condition | |
| Strains | Escherichia coli BW25273 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RcsB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | RcsB |
| Growth Condition | |
| Strains | Escherichia coli BW25274 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Rob |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | Rob |
| Growth Condition | |
| Strains | Escherichia coli BW25275 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RutR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.16/h |
| Case-specific description | RutR |
| Growth Condition | |
| Strains | Escherichia coli BW25276 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SdiA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | SdiA |
| Growth Condition | |
| Strains | Escherichia coli BW25277 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SoxR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | SoxR |
| Growth Condition | |
| Strains | Escherichia coli BW25278 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SoxS |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | SoxS |
| Growth Condition | |
| Strains | Escherichia coli BW25279 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | SspA |
| Growth Condition | |
| Strains | Escherichia coli BW25280 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TdcA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | TdcA |
| Growth Condition | |
| Strains | Escherichia coli BW25281 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TdcR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | TdcR |
| Growth Condition | |
| Strains | Escherichia coli BW25282 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 TorR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.16/h |
| Case-specific description | TorR |
| Growth Condition | |
| Strains | Escherichia coli BW25283 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UspA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.2/h |
| Case-specific description | UspA |
| Growth Condition | |
| Strains | Escherichia coli BW25284 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UvrY |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | UvrY |
| Growth Condition | |
| Strains | Escherichia coli BW25285 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 UxuR |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | UxuR |
| Growth Condition | |
| Strains | Escherichia coli BW25286 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YbhD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | YbhD |
| Growth Condition | |
| Strains | Escherichia coli BW25287 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YdeO |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | YdeO |
| Growth Condition | |
| Strains | Escherichia coli BW25288 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YdjF |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | YdjF |
| Growth Condition | |
| Strains | Escherichia coli BW25289 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 YfhA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.2/h |
| Case-specific description | YfhA |
| Growth Condition | |
| Strains | Escherichia coli BW25290 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 ElbB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | ElbB |
| Growth Condition | |
| Strains | Escherichia coli BW25291 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FecI |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | FecI |
| Growth Condition | |
| Strains | Escherichia coli BW25292 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FlgM |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | FlgM |
| Growth Condition | |
| Strains | Escherichia coli BW25293 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 FliA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.19/h |
| Case-specific description | FliA |
| Growth Condition | |
| Strains | Escherichia coli BW25294 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoD |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | RpoD |
| Growth Condition | |
| Strains | Escherichia coli BW25295 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoN |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | RpoN |
| Growth Condition | |
| Strains | Escherichia coli BW25296 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RpoS |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.16/h |
| Case-specific description | RpoS |
| Growth Condition | |
| Strains | Escherichia coli BW25297 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Rsd |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | Rsd |
| Growth Condition | |
| Strains | Escherichia coli BW25298 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RseA |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.18/h |
| Case-specific description | RseA |
| Growth Condition | |
| Strains | Escherichia coli BW25299 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 RseB |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | RseB |
| Growth Condition | |
| Strains | Escherichia coli BW25300 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Pgi |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | Pgi |
| Growth Condition | |
| Strains | Escherichia coli BW25301 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 Zwf |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.17/h |
| Case-specific description | Zwf |
| Growth Condition | |
| Strains | Escherichia coli BW25302 |
| Genotype | F-,DE(araD-araB)567,lacZ4787(del)::rrnB-3,LAM-,rph-1,DE(rhaD-rhaB)568,hsdR514 SdhC |
| Culture medium | Luria-Bertani(LB) complex medium,supplemented with 50 mg/L kanamycin for all mutants.The M9 medium contained, per liter of deionized water,the following:0.8g (NH4)2SO4,0.5g NaCl,7.5g Na2HPO4-2H2O and 3.0g KH2PO4.The following components were sterilized separately and then added (per liter of final medium):1ml of 1M MgSO4,1ml of 0.1M CaCl2, 0.6ml 0.1M FeCl3-6H2O,2ml of 1mM filter-sterilized thiamine HCl and 10ml of a trace element solution containing (per liter)0.18g ZnSO4-7H2O,0.12g CuCl2-2H2O,0.12 g MnSO4-H2O and 0.18g CoCl2-6H2O.Filter-sterilized glucose or galactose was added to a final concentration of 3g/L and 1g/L for batch and chemostat experiments,respectively. |
| Carbon source | Glactose |
| Growth rate | 0.15/h |
| Case-specific description | SdhC |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.16 |
| Acetate | 4.95 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.11 |
| Acetate | 3.92 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.74 |
| Acetate | 4.76 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.3 |
| Acetate | 3.19 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.36 |
| Acetate | 4.39 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.87 |
| Acetate | 4.64 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.28 |
| Acetate | 4.72 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.15 |
| Acetate | 4.89 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.12 |
| Acetate | 3.69 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.9 |
| Acetate | 5.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.86 |
| Acetate | 5.96 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.06 |
| Acetate | 5.12 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.37 |
| Acetate | 4.33 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.33 |
| Acetate | 4.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 5.27 |
| Acetate | 2.61 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.48 |
| Acetate | 5.31 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.13 |
| Acetate | 4.25 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.68 |
| Acetate | 4.73 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.9 |
| Acetate | 3.55 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.49 |
| Acetate | 5.19 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 9.13 |
| Acetate | 4.72 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.44 |
| Acetate | 4.65 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.2 |
| Acetate | 4.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.8 |
| Acetate | 4.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.11 |
| Acetate | 4.07 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.05 |
| Acetate | 4.55 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.31 |
| Acetate | 4.29 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.21 |
| Acetate | 4.25 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.51 |
| Acetate | 4.96 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.95 |
| Acetate | 4.91 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.77 |
| Acetate | 4.4 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.99 |
| Acetate | 4.56 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.84 |
| Acetate | 4.44 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.26 |
| Acetate | 4.52 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 4.76 |
| Acetate | 4 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.13 |
| Acetate | 4.51 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 5.11 |
| Acetate | 3.7 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.14 |
| Acetate | 4.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.03 |
| Acetate | 4.5 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.45 |
| Acetate | 3.64 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.66 |
| Acetate | 2.89 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.39 |
| Acetate | 3.8 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.32 |
| Acetate | 4.64 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.24 |
| Acetate | 4.12 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 5.52 |
| Acetate | 4.34 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.72 |
| Acetate | 4.09 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.1 |
| Acetate | 4.29 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.71 |
| Acetate | 4.12 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.3 |
| Acetate | 3.62 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.23 |
| Acetate | 4.71 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.98 |
| Acetate | 5.24 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.81 |
| Acetate | 4.42 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.41 |
| Acetate | 3.45 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.75 |
| Acetate | 4.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.42 |
| Acetate | 4.4 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.09 |
| Acetate | 3.69 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.54 |
| Acetate | 5.62 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.93 |
| Acetate | 3.86 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.03 |
| Acetate | 5.09 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.38 |
| Acetate | 4.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.65 |
| Acetate | 4.2 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.31 |
| Acetate | 4.23 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.73 |
| Acetate | 4.51 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.95 |
| Acetate | 5.9 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.85 |
| Acetate | 5.22 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.88 |
| Acetate | 3.8 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.64 |
| Acetate | 4.45 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.1 |
| Acetate | 4.42 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.21 |
| Acetate | 4.82 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.84 |
| Acetate | 4.32 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.42 |
| Acetate | 4.73 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.69 |
| Acetate | 5.16 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.5 |
| Acetate | 4.9 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.26 |
| Acetate | 4.78 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.74 |
| Acetate | 4.38 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.02 |
| Acetate | 4.18 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.73 |
| Acetate | 4 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7 |
| Acetate | 4.94 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.84 |
| Acetate | 4.85 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.96 |
| Acetate | 5.64 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.95 |
| Acetate | 4.85 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.93 |
| Acetate | 3.77 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.68 |
| Acetate | 5.13 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.1 |
| Acetate | 4.63 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.78 |
| Acetate | 4.75 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.43 |
| Acetate | 5.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.61 |
| Acetate | 4.61 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 4.12 |
| Acetate | 2.36 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.55 |
| Acetate | 4.18 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 7.6 |
| Acetate | 4.44 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.29 |
| Acetate | 5.31 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.22 |
| Acetate | 4.51 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 4.01 |
| Acetate | 1.51 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.35 |
| Acetate | 4.62 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 8.8 |
| Acetate | 7.94 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2 |
| Acetate | 0.11 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.26 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.64 |
| Acetate | 0.15 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.08 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.49 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.65 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.55 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.13 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.04 |
| Acetate | 0.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.04 |
| Acetate | 0.07 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.97 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 4.09 |
| Acetate | 0.92 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.29 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.14 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 0.8 |
| Acetate | 0.21 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.49 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.11 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.59 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.82 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.29 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.99 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.76 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.65 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.12 |
| Acetate | 0.1 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.56 |
| Acetate | 0.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.5 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.73 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.56 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.3 |
| Acetate | 0.28 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.33 |
| Acetate | 0.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.67 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.71 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.59 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.15 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.06 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.16 |
| Acetate | 0.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.32 |
| Acetate | 0.84 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.73 |
| Acetate | 0.13 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.92 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 5.27 |
| Acetate | 2.59 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 6.91 |
| Acetate | 2.29 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.23 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.02 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.17 |
| Acetate | 0.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.21 |
| Acetate | 0.15 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.16 |
| Acetate | 0.07 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.49 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.8 |
| Acetate | 0.37 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.02 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 5.5 |
| Acetate | 2.66 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.19 |
| Acetate | 0.07 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.84 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.86 |
| Acetate | 0.26 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.49 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.07 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.72 |
| Acetate | 0.16 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.12 |
| Acetate | 0.11 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.01 |
| Acetate | 0.23 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.6 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.7 |
| Acetate | 0.17 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.37 |
| Acetate | 0.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.65 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.32 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.17 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.98 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.53 |
| Acetate | 0.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.21 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.84 |
| Acetate | 0.01 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.7 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.76 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.92 |
| Acetate | 0.07 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.92 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.96 |
| Acetate | 0.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.11 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.69 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 3.02 |
| Acetate | 0.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.88 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.86 |
| Acetate | 0.19 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.87 |
| Acetate | 0 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.3 |
| Acetate | 0.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.4 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.33 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.56 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.17 |
| Acetate | 0.08 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.4 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.82 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.91 |
| Acetate | 0.05 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.78 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.35 |
| Acetate | 0.04 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.82 |
| Acetate | 0.03 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.77 |
| Acetate | 0.1 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.2 |
| Acetate | 0.02 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.61 |
| Acetate | 0.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 2.04 |
| Acetate | 0.06 |
| Specific Rate | (mmol g-1 h-1) |
| Glucose | 1.57 |
| Acetate | 2.5 |