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Table 1 Metabolic engineering of heterologous host for the production of SA

From: Metabolic rewiring of microbial cell factories for improved production of succinic acid

Engineering Strategy

Carbon substrate

Culture methods

Titer (g/L)

Productivity (g/L/h)

Yield (g/g)

By-product

Reference

Escherichia coli

 Overexpression of ppc gene expressing PEP carboxykinase

Glucose

Batch, Anaerobic

10.7

0.594

0.29

Ethanol, Lactate, Acetate, Formate

[32]

 Overexpression of heterologous pyc

Glucose

Batch, Anaerobic

1.77

0.177

0.177

Lactate, Formate

[85]

 Δldh and Δpfl gene, Overexpression of sfcA gene

Glucose

Batch, Anaerobic

12.8

0.29

0.64

Acetate Formate

[37]

 Δldh and Δpfl gene, Mutation in ptsG gene

Glucose

Fed-Batch, Dual Phase Aeration

-

0.87

0.65

Acetate, Ethanol

[40]

Glucose

Fed-Batch, Anaerobic

-

-

0.60

Acetate, Ethanol

[39]

Glucose

Fed-Batch, Anaerobic

-

-

0.88

Acetate, Ethanol

[86]

 Overexpression of pyc

Glucose

Fed-Batch, Dual Phase Aeration

99.2

1.3

1.1

Pyruvate, Formate

[40]

 Mutation in ptsG21 gene, followed by Δpfl and ΔldhA gene,

Glucose

Batch, Dual Phase Aeration

-

-

0.88

Acetate

[41]

Fructose

Batch, Dual Phase Aeration

-

-

0.44

Acetate, Formate, Malate

[41]

Glucose and Fructose (1:1)

Batch, Dual Phase Aeration

-

-

0.71

Acetate. Formate

[41]

 ΔadhE, ΔldhA genes; and overexpression of heterologous pyc from Lactococcus lactis

Glucose

Batch, Anaerobic

15.6

0.65

0.83

Formate. Acetate

[42]

 ΔptsG system

Glucose

Batch, Anaerobic

-

-

0.91

Formate. Acetate

[42]

 ΔadhE, ΔldhA, and Δack-pta, ΔiclR gene inactivation; overexpression of heterologous pyc from Lactococcus lactis

Glucose

Fed-batch, anaerobic

40

0.42

1.06

Formate. Acetate

[43]

 ΔadhE, ΔldhA, and Δack-pta; overexpression of heterologous pyc from Lactococcus lactis

Glucose

Batch, Anaerobic

15.9

0.64

1.07

Formate

[87]

 ΔiclR, ΔsdhAB, Δicd, Δ (ackA-pta), ΔpoxB

Glucose

Batch, Aerobic

4.61

0.06

0.43

Pyruvate, Acetate

[44]

Overexpression of sorghum pepc

Glucose

Batch, Aerobic

9

0.14

0.72

Pyruvate, Acetate

[44]

 ΔldhA, ΔadhE, ΔackA, ΔfocA-pflB

Glucose

Fed-batch, Anaerobic

86.6

0.9

0.92

Malate, acetate

[46]

 ΔldhA, ΔadhE, ΔackA, ΔfocA-pflB, ΔmgsA, ΔpoxB

Glucose

Fed-batch, Anaerobic

78.8

0.82

0.79

Acetate, Pyruvate, Malate

[46]

 Δpta-ackA in KJ122(ΔldhA, ΔadhE, ΔfocA-pflB, ΔmgsA, ΔpoxB, ΔtdcDE, ΔcitF, ΔaspC, ΔsfcA)

Glucose

Fed-batch, Anaerobic

71.6

0.75

1

Acetate, Pyruvate, Malate

[47]

Corynebacterium glutamicum

 ΔldhA

Glucose

Micro-aerobic, fed-batch with membrane for cell recycling

23

3.83

0.19

Lactate

[51]

 ΔldhA, Over-expressed pyc

Glucose

Two stages – aerobic growth /

Anaerobic fed-batch

146

3.17

0.92

Acetate

[52]

 ΔldhA Δpta Δpqo ΔcatPsod-ppcPsod-pyc

Expression of xylA, xylB, araE over- expression of tkt and tal

Corn stalk

Two stage, aerobic culture of biomass and anaerobic batch fermentation, minimal medium

98.6

4.29

0.87

-

[88]

 araBAD from Escherichia coli was inserted

Arabinose

Aerobic

74.4

0.36

0.58

Acetate

Pyruvate

[53]

Glucose and arabinose

 

110.2

0.28

0.56 (mol substrate)−1

Acetate

Pyruvate

 ΔldhA gene

Arabinose

Two-stage fermentation system in screw-cap tube

1.74

0.87

0.89

-

[54]

Glucose and arabinose

 

1.31

0.22

0.63

-

Glucose and Sucrose

 

3.31

0.41

1.48

-

Sucrose and Arabinose

 

2.85

0.36

1.28

-

Glucose, Sucrose and Arabinose

 

2.84

0.36

1.17

-

 Δcat, Δpqo, Δpta-ackA, ΔldhA, over-expression of native pyc and Mycobacterium vaccae fdh

Glucose

Two stages – aerobic culture/ anaerobic fed- batch production

82

1.60

0.36

Acetate

[55]

 Δcat Δpqo Δpta- ackA ΔldhA over-expression of native pyc and Mycobacterium vaccae fdh

Glucose

Two stages – aerobic culture/ anaerobic fed- batch production

134

2.48

1.67

-

[89]

 Expression of E. coli glpFKD operon

Glycerol

Fed-batch, aerobic culture

9.3

0.423

0.42

-

[56]

 ΔldhA derivative with additional in-frame deletion of NCgl2130

Glucose

Fermentation culture under microaerobic and anaerobic conditions,

8.1

3.24

0.56

-

[58]

 Corynebacterium glutamicum AJ13869DsdhA/pVK9::PmsrA-CgynfM AJ110655

Glucose

Aerobic condition

110

15

0.33

-

[59]

 Corynebacterium glutamicum FK948/pVK9::PmsrA-CgynfM (deleted sucE1 gene)

Glucose

Anaerobic condition

270

15.3

-

-

[59]

 Δldh, Δpta-ackA, ΔactA, ΔpoxB, pycP458, Δpck_Ptuf::Ms.pckG, Ptuf::ppc, ΔptsG

Over-expression of NCgl0275

Glucose

One stage – aerobic culture/anaerobic fed- batch production

152.2

1.11

1.10

-

[90]

 ΔaceE Δpqo ΔldhA ΔC-T ilvN ΔalaT ΔavtA

ΔPDHC, ΔPQO

Glucose

One stage fed-batch fermentation

38.9

0.66

0.67

Pyruvate

[91]

 BL-1 harboring pBbEB1c-torA-SbAmyA

Micro-algal starch

Minimal medium

Sequential aerobic fermentations of CO2-grown micro-algae and engineered C. glutamicum

0.5

0.021

0.28

-

[92]

 ΔldhA

chromosomal integration into the pta-ackA locus of xylA and xylB gene from E. coli

Corn cob

Hydrolysate (Xylose + Glucose), bi-carbonate

Two-stage, aerobic culture of biomass and anaerobic batch fermentation, minimal medium

40.8

0.85

0.69 (mol/mol)

Acetate, Pyruvate

[93]

 Expression of acetyl-CoA synthetase

Over-expression of gltA gene (citrate synthase)

Glucose

Minimal medium

Aerobic growth

Fed-batch culture

241 (mM)

3.55

(mM h−1)

0.62 (mol/mol)

-

[57]

Saccharomyces cerevisiae

 Δsdh2, Δsdh1, Δidh1, Δidp1

Glucose

Batch,

Aerobic

3.62

0.022

0.072

Ethanol, Glycerol, Acetate

[65]

 Δsdh3, Δser3, Δser33

Glucose

Batch, Aerobic

0.60

-

0.03

-

[69]

 Evolved 8D with icl1

Glucose

Batch, Aerobic

0.90

-

0.05

-

[69]

Yarrowia lipolytica

 Δsdh5

Crude glycerol

Aerobic Fed-batch

160

0.4

0.4

Acetic acid

[94]

 sΔsdh5, overexpression of ScPCK, YlSCS2

Glycerol

Aerobic Fed-batch

110.7

-

0.53

Mannitol

[84]

 Δsdh5, overexpression of XR, XDH, XK

Xylose

Aerobic Fed-Batch

22.3

-

0.15

Acetic acid

[95]