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Table 1 Some examples of SA bio-production systems using natural producers or metabolic engineered organisms

From: Reconstruction of a genome-scale metabolic model for Actinobacillus succinogenes 130Z

Organism

Genetic modifications

Culture conditions

Carbon sources (CS)

SA Yield

(g.gCS−1)

References

B. succiniciproducens

 

Anaerobic, continuous

Glycerol

1.02

[21]

M. succiniproducens

 

Anaerobic, batch

Glucose

0.59

[71]

M. succiniproducens

– Deletion of ldhA, pflB, pta, and ackA genes

Anaerobic, fed-batch

Glucose

0.76

[30]

A. succinogenes

 

Anaerobic, continuous

Xylose

0.80

[63]

A. succinogenes

 

Anaerobic, batch

Glucose

0.74

[72]

A. succinogenes

 

Anaerobic, repeated fed-batch

Glucose

0.88

[31]

E. coli

– Deletion of pflB, ldhA, ppc genes

– Heterologous expression of pckA from B. subtilis

Anaerobic, batch

Corn stalk hydrolysate

1.02

[43]

E. coli

– Deletion of iclR, icd, sdhAB, ackA-pta, poxB

– Heterologous expression of pepc gene from Sorghum vulgare

Aerobic, batch

Glucose

0.72

[73]

S. cerevisiae

– Deletion of sdh3, ser3, ser33

– Overexpression of ICL1

Aerobic, batch

Glucose

0.05

[37]

S. cerevisiae

– Deletion of pdc1, pdc5, pdc6, fum1, gpd1

– Overexpression of pyc2, mdh3, fumC and frds1

Aerobic, batch

Glucose

0.14

[19]

  1. Mass yields are given in g.g− 1 of carbon source (CS)