Product | Host | Engineering genes | Specific modification | Titer productivity | References |
---|---|---|---|---|---|
Isobutanol | S. elongatus | alsS ilvC ilvD in NSII kivD yqhD in NSI | Initial OD730 at 1.0 Enhancing rubisco | 450Â mg/L 150Â mg/L/OD | [11] |
Isobutanol | Synechocystis | kivD adhA | Mixotrophic condition In situ removal of isobutanol | 298Â mg/L 24.8Â mg/L/OD | [23] |
Isobutanol | S. elongatus | alsS ilvC ilvD in NSII kivD yqhD in NSI | Deleting a glgC gene | 550Â mg/L 122Â mg/L/OD | [22] |
Isobutanol | Synechocystis | alsS ilvC ilvD kivD slr1192 | HCl-titrated culture | 911Â mg/L 227Â mg/L/OD | [24] |
Isobutanol | Synechocystis | kivD slr1192 | Addition of isobutyraldehyde | 290Â mg/L 72.5Â mg/L/OD | [33] |
Isobutanol | S. elongatus | alsS ilvC ilvD kivD adhA in NSI | High salinity stress | 637Â mg/L 290Â mg/L/OD | This study |
n-Butanol | S. elongatus | ter in NSI atoB adhE2 crt hbd in NSII | Anoxic condition | 14.5Â mg/L 5.8Â mg/L/OD | [7] |
n-Butanol | S. elongatus | ter in NSI nphT7 bldh yqhD phaJ phaB in NSII | Engineering ATP consumption | 30Â mg/L 6.0Â mg/L/OD | [8] |
n-Butanol | Synechocystis | ter phaJ pduP nphT7 fadB slr1192 | Modular pathway engineering | 836Â mg/L 199Â mg/L/OD | [10] |
n-Butanol | S. elongatus | ter in NSI nphT7 pduP yqhD phaJ phaB in NSII | Using oxygen-tolerant PduP | 404Â mg/L 66.7Â mg/L/OD | [9] |