Table 3.
Production of fuels and chemicals using native or synthetic methylotrophic bacteria.
Product |
Strain |
Methanol assimilation pathway |
Metabolic engineering strategy |
Substrate |
Culture condition |
Product titer/yield |
Ref. |
---|---|---|---|---|---|---|---|
Native methylotrophic bacteria | |||||||
L-glutamate | B. methanolicus | RuMP | Δhom-1 | Methanol | Fed-batch fermentation with automatic control for methanol feeding | 32 g/l | [42] |
Methanol and methionine | Fed-batch fermentation with automatic control for methanol along with methionine feeding | 69 g/l | |||||
L-lysine | B. methanolicus | RuMP | NOA2 mutant strain | Methanol and amino acids | Fed-batch fermentation with automatic control for methanol supply; supplementation of threonine, lysine, and methionine | 65 g/l | [42] |
Cadaverine | B. methanolicus | RuMP | Heterologous expression of cadA and ldcC; overexpression of l-lysine synthesis pathway | Methanol | Fed-batch fermentation using methanol as the sole carbon source | 11.3 g/l | [44] |
5-AVA | B. methanolicus | RuMP | Expression of 5-AVA biosynthesis pathway from cadaverine and l-lysine | Methanol | Shake flask cultures using methanol as the sole carbon source | 23.7 mg/l | [45] |
Methanol andcadaverine | Shake flask cultures using methanol along with supplementation of cadaverine | 77 mg/l | |||||
GABA | B. methanolicus | RuMP | Heterologous expression of gadSt and gadB | Methanol | Fed-batch fermentation employing a pH shift from 6.5 to 4.6 using methanol as the sole carbon source | 9 g/l | [46] |
Acetoin | B. methanolicus | RuMP | Heterologous expression of alsSD operon, overexpression of malic enzyme, and isocitrate lyase | Methanol | Shake flask using methanol as the carbon source | 0.42 g/l | [57] |
2-HIBA | M. extorquens AM1 | Serine cycle | Expression of B12-dependent mutases | Methanol | Fed-batch fermentation using methanol as the sole carbon source under nitrogen-limiting conditions | 2.1 g/l | [53] |
α-humulene | M. extorquens AM1 | Serine cycle | Heterologous expression of α-humulene synthase and FFP; heterologous expression of the mevalonate pathway | Methanol | Fed-batch fermentation using methanol as the sole carbon source, cumate as inducer, and dodecane as an organic overlay | 1.65 g/l | [64] |
Itaconic acid | M. extorquens AM1 | Serine cycle | Heterologous expression of cis-aconitic acid decarboxylase; repression of phaR | Methanol | Fed-batch fermentation using methanol as the sole carbon source | 31.6 mg/l | [56] |
Violacein | M. extorquens AM1 | Serine cycle | Heterologous expression of operon VioABCDE followed by random mutagenesis | Methanol | Shake flask cultures using methanol as the sole carbon source | 67.8 mg/l | [65] |
Methanol and acetate | Shake flask cultures using methanol and acetate | 118 mg/l | |||||
Mesaconic acid | M. extorquens AM1 | Serine cycle | Expression of yciA (thioestrase) | Methanol | Shake flask using methanol as the sole carbon source | 70 mg/l | [54] |
3-Hydroxypropionic acid | M. extorquens AM1 | Serine cycle | Heterologous expression of mcr; enhancing the expression by promoter optimization and multicopy expression of mcr | Methanol | Shake flask using methanol as the sole carbon source | 69.8 mg/l | [58] |
Mevalonate | M. extorquens AM1 | Serine cycle | Construction of mevalonate biosensor along with mevalonate biosynthesis pathway | Methanol | Fed-batch fermentation using methanol as the sole carbon source | 2.67 g/l | [61] |
Crotyl diphosphate | M. extorquens AM1 | Serine cycle | Expression of THKM82V, IPK and ADH2 | Methanol and crotonol | Shake flask using methanol along with supplementation of exogenous crotonal | 0.60 μg/mL | [135] |
Crotonic acid | M. extorquens AM1 | Serine cycle | Heterologous expression of isocitrate lyase and malate synthase for activation of the glyoxylate shunt, deletion of EMC pathway genes | Methanol | Shake flask using methanol as the sole carbon source | Growth defects on sole methanol | [55] |
Acetate | Shake flasks using initial growth on acetate; supplementation of 3-nitropropionate to repress glyoxylate shunt during production phase on acetate | 0.2 mg/l | |||||
PHB | M. extorquens sp. K. | Serine cycle | N/A | Methanol | Fed-batch fermentation using methanol as the sole carbon source under nitrogen and mineral salt-deficient conditions | 136 g/l; 66% of total DCW | [49] |
P(3HB-co-3HV-co-3HHX) | M. extorquens AM1 | Serine cycle | Deletion of native phaC, heterologous expression of phaC from Aeromonas cavaie, overexpression of β-ketothiolase and acetoacetyl-CoA reductase | Methanol | Fed-batch fermentation using methanol as the sole carbon source under cobalt-deficient conditions | 43.6% of DCW | [136] |
PHB | M. extorquens AM1 | Serine cycle | N/A | Methanol | Fed-batch fermentation with controlled methanol supplementation (0.01 g/l) in minimal media | 46% of DCW | [48] |
P(3HB-co-3HV) | Methylobacterium sp. GW2 | Serine cycle | N/A | Methanol and valerate | Fed-batch fermentation using 0.5% methanol as carbon source; supplementation of valerate | 30% of DCW | [50] |
Synthetic methylotrophic bacteria | |||||||
Succinic Acid | E. coli | RuMP | Heterologous expression of NAD-dependent MDH; heterologous expression of RuMP pathway | Glucose and methanol | Fed-batch fermentation using 100 g/l glucose and 6.4 g/l methanol. Methanol was used as an auxiliary substrate | 68.75 g/l, 1.45% carbon derived from methanol | [113] |
Ethanol | E. coli | Modified Serine cycle | Deletion of aceB, gcvP, glcB, frdB, ldhA, gcl, expression of the modified serine cycle, expression of the ethanol production pathway | LB, methanol, and xylose | Shake flask using LB medium supplemented with 30 mM xylose and 200 mM methanol | 36.3 mM, 33.8% of carbon derived from methanol | [117] |
Acetate | E. coli | Modified Serine cycle | ΔaceB, ΔgcvP, ΔglcB, ΔfrdB, ΔldhA, Δgcl, expression of modified serine cycle, expression of the ethanol production pathway | LB, methanol, and xylose | Shake flask using LB medium supplemented with 30 mM xylose and 200 mM methanol | 37 mM, 27.2% of carbon derived from methanol | [117] |
1-butanol | E. coli | RuMP | Δrpe, ΔrpiAB, expression of NAD-dependent MDH, Hps, and Phi followed by adaptive evolution, expression of the 1-butanol production pathway | Xylose and methanol | Fed-batch fermentation using 87 mM of methanol and 100 mM of xylose | 2.0 g/L, 71% of carbon derived from methanol | [137] |
Acetone | E. coli | RuMP | Δpgi, ΔfrmA, Expression of MDH, Hps, and Phi, Expression of non-oxidative pentose phosphate pathway; expression of acetone formation pathway |
Glucose and methanol | Fed-batch fermentation using 260 mM glucose and 38.3 mM methanol | 45.0 mM, 3.6% of carbon derived from methanol | [75] |
E. coli | Δpgi, ΔrpiAB, Δedd, ΔfrmA, expression of RuMP pathway followed by ALE | Glucose and methanol | Fed-batch fermentation using 36 g/l glucose and 500 mM methanol | 1 g/L, 22% of carbon derived from methanol | [138] | ||
Cadaverine | C. glutamicum | RuMP | Δald, Δfdh; heterologous expression of NAD-dependent MDH, Hps, and Phi | Ribose and methanol | Shake flask using 20 mM ribose and 200 mM | 1.5 g/l, 15% of carbon derived from methanol | [119] |
Naringenin | E. coli | RuMP | Expression of NAD-dependent Mdh fromBacillus stearothermophilus, Expression of Hps and Phi from B. methanolicus, Expression of Coumaroyl CoA ligase and Chalcone synthase | Co-utilization of methanol and yeast extract | 3.5 mg/L 18% of carbon derived from methanol | [139] | |
D-allulose | E. coli | RuMP | Coupling of allulose monophosphate, RuMP, and PPP | Xylose and methanol | Fed-batch fermenter using 102 mM xylose and 97 mM methanol in the presence of yeast extract and tryptone | 0.512 mM d-allulose/mM methanol | [116] |
Succinic Acid | E. coli | RuMP | Expression of methanol dissimilation pathway along with RuMP pathway | Glucose, methanol, and formate | Fed-batch using 50 g/l glucose, 2 g/l formate, and 200 mM methanol. Methanol and formate were used as auxiliary substrates | 63.42 g/l | [114] |