From: Metabolic engineering strategy for synthetizing trans-4-hydroxy-l-proline in microorganisms
Host strain | Expression vectors | Metabolic engineering strategies | Titer (g/L) | Culture system | References |
---|---|---|---|---|---|
E. coli | pTr2-4OH | (1) + Da-p4ho; (2) promoterso; and (3)ΔputA; | 41 | Batch, 5 L (glucose + proline) | [58] |
E. coli | pSTV29 | (1) + Da-p4h; (2) + proB*; (3) + proA; and (4)ΔputA | 25 | Batch, 5 L (glucose) | [38] |
E. coli and C. glutamicum | pET28a | Compared with the Ps-p4h and Bo-p4h, and Da-p4h | 2.28 or 6.72 | Batch, 250 mL(glucose) or Batch, 250 mL (glucose + proline) | [19] |
C. glutamicum | pEKEx2 | + p4h | 7.1 | Fed-batch, 3 L (glucose + isoleucine) | [70] |
E. coli | pUC19 | (1) + Da-p4ho; (2) expression vectorso; | 25.4 | Fed-batch, 5 L (glycerol + proline) | [81] |
E. coli | pTrc99a | (1) + Da-p4h; and (2) + VHb | 14.4 | Fed-batch, 1.4 L (glucose + proline) | [75] |
E. coli | pTrc99a | (1) + Da-p4h; (2)ΔsucAB; (3)ΔaceAK; (4)ΔputA; and (5) + proB*; and (6) + proA gene | 31 | Fed-batch, 5 L (glucose) | [67] |
E. coli | pTc | (1) + p4hgm; (2)ΔputA; (3) + proB*; and (4) + proA | 45.83 | Fed-batch, 5 L (glucose) | [55] |
C. glutamicum | pXMJ19 | (1) + Da-p4h; (2)ΔsucCD; and (3) fine-tuning of proB* and p4h abundances | 21.72 | Fed-batch, 500 mL (glucose) | [62] |
E. coli | pET21a | (1) + Un-p4h; (2) + p4hre; (3) p4h*; (4)ΔputA; (5) + proB*; and (6) + proA | 12.9 | Fed-batch, 5 L (glucose) | [57] |
E. coli | pDXW-10 | (1) + p4hrd; (2) + p4ho; (3)ΔputA; (4)ΔproP; (5)ΔputP; (6)ΔaceA; (7) + proB*; and (8) a tunable circuit based on quorum sensing | 54.8 | Fed-batch, 7.5 L (glucose) | [69] |