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 | 708.4 | -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 | 640.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.7 | R02736+R01528 |
| ATP production rate Maximum | 632.15 | -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 | 594.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 59.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.4 | R02736+R01528 |
| ATP production rate Maximum | 689.8 | -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 | 649.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.4 | R02736+R01528 |
| ATP production rate Maximum | 929.7 | -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 | 821.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 34.9 | R02736+R01528 |
| ATP production rate Maximum | 929.85 | -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 | 789.35 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 106.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.2 | R02736+R01528 |
| ATP production rate Maximum | 938.4 | -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 | 821.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 85.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.7 | R02736+R01528 |
| ATP production rate Maximum | 923.8 | -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 | 791.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 96.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.7 | R02736+R01528 |
| ATP production rate Maximum | 653.35 | -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 | 604.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.9 | R02736+R01528 |
| ATP production rate Maximum | 717.95 | -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 | 636.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 81.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.8 | R02736+R01528 |
| ATP production rate Maximum | 988 | -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 | 836.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 97.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36.6 | R02736+R01528 |
| ATP production rate Maximum | 789.35 | -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 | 717.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 35.7 | R02736+R01528 |
| ATP production rate Maximum | 504.95 | -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 | 382.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.4 | R02736+R01528 |
| ATP production rate Maximum | 782.2 | -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 | 705.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.8 | R02736+R01528 |
| ATP production rate Maximum | 622.5 | -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 | 568.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 85.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 63.9 | R02736+R01528 |
| ATP production rate Maximum | 920.5 | -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 | 708.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 137 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.2 | R02736+R01528 |
| ATP production rate Maximum | 684.3 | -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 | 591.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.5 | R02736+R01528 |
| ATP production rate Maximum | 706.2 | -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 | 620.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 87.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 53.7 | R02736+R01528 |
| ATP production rate Maximum | 1030.05 | -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 | 882.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 97.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.6 | R02736+R01528 |
| ATP production rate Maximum | 735.2 | -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 | 666.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.6 | R02736+R01528 |
| ATP production rate Maximum | 728.3 | -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 | 687.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 51.4 | R02736+R01528 |
| ATP production rate Maximum | 628.5 | -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 | 586 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49 | R02736+R01528 |
| ATP production rate Maximum | 735.85 | -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 | 680.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.9 | R02736+R01528 |
| ATP production rate Maximum | 734.15 | -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 | 677.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 700 | -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 | 623.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.9 | R02736+R01528 |
| ATP production rate Maximum | 543.8 | -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 | 500.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 62 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.7 | R02736+R01528 |
| ATP production rate Maximum | 576.15 | -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 | 530.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49 | R02736+R01528 |
| ATP production rate Maximum | 652.95 | -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 | 609.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.6 | R02736+R01528 |
| ATP production rate Maximum | 795 | -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 | 697 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 92.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.9 | R02736+R01528 |
| ATP production rate Maximum | 615.4 | -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 | 548.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 58.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 31.8 | R02736+R01528 |
| ATP production rate Maximum | 679.35 | -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 | 616.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 53 | R02736+R01528 |
| ATP production rate Maximum | 650.45 | -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 | 606.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.2 | R02736+R01528 |
| ATP production rate Maximum | 582.1 | -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 | 544.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 55 | R02736+R01528 |
| ATP production rate Maximum | 650.35 | -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 | 592.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 51.6 | R02736+R01528 |
| ATP production rate Maximum | 715.95 | -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 | 631.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 33.8 | R02736+R01528 |
| ATP production rate Maximum | 826.8 | -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 | 707.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.1 | R02736+R01528 |
| ATP production rate Maximum | 830.3 | -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 | 720.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 81.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.8 | R02736+R01528 |
| ATP production rate Maximum | 963.5 | -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 | 815.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 84.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 25.5 | R02736+R01528 |
| ATP production rate Maximum | 661.75 | -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 | 610 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.7 | R02736+R01528 |
| ATP production rate Maximum | 600.5 | -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 | 536 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49.5 | R02736+R01528 |
| ATP production rate Maximum | 918 | -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 | 700.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 120.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 33.3 | R02736+R01528 |
| ATP production rate Maximum | 959.75 | -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 | 728.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 125.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 33.1 | R02736+R01528 |
| ATP production rate Maximum | 777.1 | -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 | 689.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 85.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.2 | R02736+R01528 |
| ATP production rate Maximum | 1086.15 | -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 | 924.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 117.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.8 | R02736+R01528 |
| ATP production rate Maximum | 771.65 | -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 | 698.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.5 | R02736+R01528 |
| ATP production rate Maximum | 664.3 | -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 | 592.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 57.4 | R02736+R01528 |
| ATP production rate Maximum | 655.7 | -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 | 610.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49 | R02736+R01528 |
| ATP production rate Maximum | 608.6 | -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 | 564.35 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.2 | R02736+R01528 |
| ATP production rate Maximum | 1028.45 | -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 | 798.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 131 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39 | R02736+R01528 |
| ATP production rate Maximum | 578.2 | -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 | 533.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.1 | R02736+R01528 |
| ATP production rate Maximum | 509.05 | -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 | 397.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 97.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.6 | R02736+R01528 |
| ATP production rate Maximum | 741.35 | -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 | 676.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.8 | R02736+R01528 |
| ATP production rate Maximum | 822.05 | -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 | 736.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.4 | R02736+R01528 |
| ATP production rate Maximum | 650.75 | -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 | 602.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 57.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.6 | R02736+R01528 |
| ATP production rate Maximum | 693.4 | -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 | 638.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.9 | R02736+R01528 |
| ATP production rate Maximum | 875.5 | -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 | 760.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 91.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.2 | R02736+R01528 |
| ATP production rate Maximum | 657.8 | -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 | 619.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 57.5 | R02736+R01528 |
| ATP production rate Maximum | 881 | -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 | 733.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 95.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36.7 | R02736+R01528 |
| ATP production rate Maximum | 660.5 | -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 | 599.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.2 | R02736+R01528 |
| ATP production rate Maximum | 652.15 | -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 | 576.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.5 | R02736+R01528 |
| ATP production rate Maximum | 668.75 | -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 | 631.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 57.3 | R02736+R01528 |
| ATP production rate Maximum | 658.65 | -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 | 591.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 79.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.4 | R02736+R01528 |
| ATP production rate Maximum | 960.55 | -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 | 877.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 82.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49.1 | R02736+R01528 |
| ATP production rate Maximum | 790.7 | -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 | 701.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 82.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.8 | R02736+R01528 |
| ATP production rate Maximum | 663.55 | -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 | 598.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.7 | R02736+R01528 |
| ATP production rate Maximum | 743.85 | -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 | 678.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.9 | R02736+R01528 |
| ATP production rate Maximum | 878.85 | -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 | 767.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 93.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.7 | R02736+R01528 |
| ATP production rate Maximum | 815 | -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 | 725.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 51.2 | R02736+R01528 |
| ATP production rate Maximum | 1199.15 | -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 | 1037.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 102.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.9 | R02736+R01528 |
| ATP production rate Maximum | 782.1 | -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 | 678.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.1 | R02736+R01528 |
| ATP production rate Maximum | 618.2 | -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 | 561.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.2 | R02736+R01528 |
| ATP production rate Maximum | 625.35 | -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 | 560.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 65.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.9 | R02736+R01528 |
| ATP production rate Maximum | 721.2 | -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 | 654.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.7 | R02736+R01528 |
| ATP production rate Maximum | 822.25 | -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 | 753.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.7 | R02736+R01528 |
| ATP production rate Maximum | 791.15 | -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 | 690.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 90.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.7 | R02736+R01528 |
| ATP production rate Maximum | 655.05 | -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 | 607.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.6 | R02736+R01528 |
| ATP production rate Maximum | 770.3 | -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 | 680.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 86.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.9 | R02736+R01528 |
| ATP production rate Maximum | 750.7 | -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 | 682.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 48.6 | R02736+R01528 |
| ATP production rate Maximum | 603.15 | -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 | 554.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.2 | R02736+R01528 |
| ATP production rate Maximum | 899.15 | -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 | 793.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 80.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.5 | R02736+R01528 |
| ATP production rate Maximum | 673.2 | -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 | 607.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.3 | R02736+R01528 |
| ATP production rate Maximum | 939.8 | -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 | 810.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 91.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.4 | R02736+R01528 |
| ATP production rate Maximum | 870.25 | -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 | 750 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 92.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.2 | R02736+R01528 |
| ATP production rate Maximum | 626.5 | -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 | 588.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 65.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.6 | R02736+R01528 |
| ATP production rate Maximum | 578.35 | -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 | 532.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 62.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.5 | R02736+R01528 |
| ATP production rate Maximum | 777.75 | -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 | 711.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 65.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.3 | R02736+R01528 |
| ATP production rate Maximum | 606.75 | -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 | 561.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 58.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.5 | R02736+R01528 |
| ATP production rate Maximum | 686.55 | -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 | 632.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.2 | R02736+R01528 |
| ATP production rate Maximum | 611.95 | -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 | 554.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.2 | R02736+R01528 |
| ATP production rate Maximum | 634.5 | -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 | 582.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 53.6 | R02736+R01528 |
| ATP production rate Maximum | 664.75 | -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 | 603.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.8 | R02736+R01528 |
| ATP production rate Maximum | 797.25 | -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 | 730.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.9 | R02736+R01528 |
| ATP production rate Maximum | 609.85 | -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 | 568.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 47.9 | R02736+R01528 |
| ATP production rate Maximum | 512 | -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 | 462 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 201.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 181.3 | R02736+R01528 |
| ATP production rate Maximum | 1116.75 | -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 | 896.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 101.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 13.1 | R02736+R01528 |
| ATP production rate Maximum | 310.75 | -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 | 274.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 60.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46.1 | R02736+R01528 |
| ATP production rate Maximum | 416.6 | -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 | 337.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39 | R02736+R01528 |
| ATP production rate Maximum | 460.75 | -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 | 363.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 82.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.4 | R02736+R01528 |
| ATP production rate Maximum | 409.45 | -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 | 329.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.6 | R02736+R01528 |
| ATP production rate Maximum | 512.6 | -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 | 405.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 35.6 | R02736+R01528 |
| ATP production rate Maximum | 450.3 | -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 | 369.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.8 | R02736+R01528 |
| ATP production rate Maximum | 444.3 | -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 | 354.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.4 | R02736+R01528 |
| ATP production rate Maximum | 395.7 | -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 | 328.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.4 | R02736+R01528 |
| ATP production rate Maximum | 423.75 | -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 | 344.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.4 | R02736+R01528 |
| ATP production rate Maximum | 379.95 | -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 | 299.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.6 | R02736+R01528 |
| ATP production rate Maximum | 399.5 | -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 | 330.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.4 | R02736+R01528 |
| ATP production rate Maximum | 415.15 | -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 | 347.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.2 | R02736+R01528 |
| ATP production rate Maximum | 370.1 | -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 | 299.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 65.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.4 | R02736+R01528 |
| ATP production rate Maximum | 415.5 | -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 | 333.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.8 | R02736+R01528 |
| ATP production rate Maximum | 442.95 | -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 | 351.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.4 | R02736+R01528 |
| ATP production rate Maximum | 405.45 | -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 | 325.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.6 | R02736+R01528 |
| ATP production rate Maximum | 396.8 | -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 | 319.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.8 | R02736+R01528 |
| ATP production rate Maximum | 421.7 | -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 | 338.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.6 | R02736+R01528 |
| ATP production rate Maximum | 392.2 | -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 | 323.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 35.6 | R02736+R01528 |
| ATP production rate Maximum | 423.85 | -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 | 344.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.6 | R02736+R01528 |
| ATP production rate Maximum | 378.4 | -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 | 316.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.4 | R02736+R01528 |
| ATP production rate Maximum | 416.45 | -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 | 336.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38 | R02736+R01528 |
| ATP production rate Maximum | 389.65 | -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 | 322.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.2 | R02736+R01528 |
| ATP production rate Maximum | 399.25 | -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 | 318 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 35.6 | R02736+R01528 |
| ATP production rate Maximum | 379 | -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 | 293 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.8 | R02736+R01528 |
| ATP production rate Maximum | 389.7 | -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 | 312.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45.2 | R02736+R01528 |
| ATP production rate Maximum | 402.15 | -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 | 320.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 408.15 | -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 | 335.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.4 | R02736+R01528 |
| ATP production rate Maximum | 422.8 | -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 | 333.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.6 | R02736+R01528 |
| ATP production rate Maximum | 357.65 | -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 | 298.65 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 60.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.2 | R02736+R01528 |
| ATP production rate Maximum | 462.9 | -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 | 370.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.8 | R02736+R01528 |
| ATP production rate Maximum | 402.1 | -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 | 318.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.4 | R02736+R01528 |
| ATP production rate Maximum | 421.45 | -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 | 339.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41 | R02736+R01528 |
| ATP production rate Maximum | 378 | -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 | 314 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.6 | R02736+R01528 |
| ATP production rate Maximum | 393.45 | -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 | 322.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 34.8 | R02736+R01528 |
| ATP production rate Maximum | 377.75 | -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 | 310.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 79.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 52.4 | R02736+R01528 |
| ATP production rate Maximum | 417.6 | -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 | 345.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.8 | R02736+R01528 |
| ATP production rate Maximum | 395.6 | -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 | 320.35 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36 | R02736+R01528 |
| ATP production rate Maximum | 471.1 | -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 | 381.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.6 | R02736+R01528 |
| ATP production rate Maximum | 369.7 | -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 | 306.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.2 | R02736+R01528 |
| ATP production rate Maximum | 510.4 | -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 | 411.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 31.4 | R02736+R01528 |
| ATP production rate Maximum | 591 | -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 | 471.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 89.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.4 | R02736+R01528 |
| ATP production rate Maximum | 370.05 | -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 | 305.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.2 | R02736+R01528 |
| ATP production rate Maximum | 425.85 | -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 | 349.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.2 | R02736+R01528 |
| ATP production rate Maximum | 382.2 | -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 | 308.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.8 | R02736+R01528 |
| ATP production rate Maximum | 387.2 | -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 | 317.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 79.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 51.8 | R02736+R01528 |
| ATP production rate Maximum | 418 | -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 | 326 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 411.35 | -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 | 325.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 35.2 | R02736+R01528 |
| ATP production rate Maximum | 399.4 | -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 | 322.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.4 | R02736+R01528 |
| ATP production rate Maximum | 415.25 | -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 | 336.25 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.2 | R02736+R01528 |
| ATP production rate Maximum | 357.6 | -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 | 300.35 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 63.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41 | R02736+R01528 |
| ATP production rate Maximum | 378.35 | -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 | 302.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.8 | R02736+R01528 |
| ATP production rate Maximum | 422.4 | -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 | 339.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 34 | R02736+R01528 |
| ATP production rate Maximum | 462.2 | -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 | 367.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 81.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.8 | R02736+R01528 |
| ATP production rate Maximum | 438.4 | -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 | 346.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 78.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 409.4 | -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 | 327.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 70 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.4 | R02736+R01528 |
| ATP production rate Maximum | 429.75 | -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 | 337 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.6 | R02736+R01528 |
| ATP production rate Maximum | 420.35 | -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 | 352.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 50.2 | R02736+R01528 |
| ATP production rate Maximum | 534.45 | -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 | 417.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 85.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39 | R02736+R01528 |
| ATP production rate Maximum | 413.3 | -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 | 336.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.4 | R02736+R01528 |
| ATP production rate Maximum | 374.2 | -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 | 312.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43 | R02736+R01528 |
| ATP production rate Maximum | 460.7 | -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 | 351.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 85.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42 | R02736+R01528 |
| ATP production rate Maximum | 433.45 | -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 | 342.7 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 74.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38 | R02736+R01528 |
| ATP production rate Maximum | 370.85 | -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 | 306.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 65.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.2 | R02736+R01528 |
| ATP production rate Maximum | 358.6 | -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 | 302.6 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42 | R02736+R01528 |
| ATP production rate Maximum | 445.4 | -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 | 354.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 77.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.4 | R02736+R01528 |
| ATP production rate Maximum | 405.75 | -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 | 326.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.8 | R02736+R01528 |
| ATP production rate Maximum | 387.6 | -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 | 314.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43 | R02736+R01528 |
| ATP production rate Maximum | 456.05 | -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 | 362.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.2 | R02736+R01528 |
| ATP production rate Maximum | 389 | -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 | 315.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.8 | R02736+R01528 |
| ATP production rate Maximum | 381.2 | -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 | 308.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.4 | R02736+R01528 |
| ATP production rate Maximum | 409.95 | -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 | 323.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 79 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.6 | R02736+R01528 |
| ATP production rate Maximum | 413.2 | -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 | 334.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 37.8 | R02736+R01528 |
| ATP production rate Maximum | 401.55 | -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 | 327.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39 | R02736+R01528 |
| ATP production rate Maximum | 404.05 | -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 | 329.05 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.4 | R02736+R01528 |
| ATP production rate Maximum | 426.65 | -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 | 342.9 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 69.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36.2 | R02736+R01528 |
| ATP production rate Maximum | 402.45 | -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 | 314.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 389 | -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 | 316 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 75.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 46 | R02736+R01528 |
| ATP production rate Maximum | 389.8 | -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 | 328.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.2 | R02736+R01528 |
| ATP production rate Maximum | 375.3 | -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 | 314.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 64.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.2 | R02736+R01528 |
| ATP production rate Maximum | 409.75 | -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 | 329.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 73.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 41.2 | R02736+R01528 |
| ATP production rate Maximum | 382.85 | -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 | 317.35 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 39.8 | R02736+R01528 |
| ATP production rate Maximum | 388.85 | -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 | 306.85 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 43.8 | R02736+R01528 |
| ATP production rate Maximum | 418.05 | -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 | 338.8 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 68.1 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36.4 | R02736+R01528 |
| ATP production rate Maximum | 434.95 | -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 | 333.45 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 83.4 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.8 | R02736+R01528 |
| ATP production rate Maximum | 409.05 | -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 | 342.55 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 40.2 | R02736+R01528 |
| ATP production rate Maximum | 435.3 | -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 | 346.3 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 36.4 | R02736+R01528 |
| ATP production rate Maximum | 378.2 | -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 | 311.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 71.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 45 | R02736+R01528 |
| ATP production rate Maximum | 344.2 | -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 | 275.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 76.5 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 49.2 | R02736+R01528 |
| ATP production rate Maximum | 392 | -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 | 318.5 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 67.8 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.4 | R02736+R01528 |
| ATP production rate Maximum | 415.35 | -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 | 340.1 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 72.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 42.2 | R02736+R01528 |
| ATP production rate Maximum | 392.75 | -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 | 322.75 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66.6 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.6 | R02736+R01528 |
| ATP production rate Maximum | 382.7 | -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 | 310.95 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 66.9 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 38.2 | R02736+R01528 |
| ATP production rate Maximum | 256.65 | -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 | 206.15 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 184.2 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 164 | R02736+R01528 |
| ATP production rate Maximum | 465.65 | -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 | 390.4 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 49.3 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 19.2 | R02736+R01528 |
| ATP production rate Maximum | 276.95 | -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 | 246.2 | -R01786-R04779+2.5*R01061+R01512+R00200+2.5*R00209 +2.5*R08549-R00405+1.5*R00402+2.5*R00342 |
| NADPH production rate Maximum | 56.7 | R02736+R01528+R00267+R00214 |
| NADPH production rate Minium | 44.4 | 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 |