Table 1.
Reference | Pdc− phenotype | Relieve Crabtree effect through ALE | Alternate acetyl-CoA routes | NAD+ regeneration | Metabolic control of ethanol production | Alternate carbon source | Product(s) | Yield (g/g carbon source) | Titer (g/L) | Conditions (carbon source, medium, batch/fed-batch, vessel, conditions) |
---|---|---|---|---|---|---|---|---|---|---|
[71] | ✓ | ✓ | ✓ | Acetate | 0.14a | < 0.5 | Glucose, minimal medium, batch, flask, aerobic | |||
Pyruvate | 0.007a | < 0.5 | ||||||||
[25] | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.28 | 96.2 | Glucose, YP medium, fed-batch, bioreactor, aerobic | |||
Glycerol | 0.09a | >30c | ||||||||
Acetoin | 0.01a | ~5c | ||||||||
[33] | ✓ | ✓ | 2,3-Butanediol | 0.407 | 72.91 | Glucose, YP medium, fed-batch, flask, aerobic | ||||
Acetoin | 0.01a | 1.38 | ||||||||
[34] | ✓ | ✓ | 2,3-Butanediol | 0.359 | 32.31c | Glucose + ethanol, minimal media, batch, bioreactor, oxygen-limited | ||||
Glycerol | 0.069 | 6.21c | ||||||||
Acetoin | 0.052 | 4.68c | ||||||||
[35] | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.404 | 154.3 | Glucose, YP medium, fed-batch, bioreactor, full aeration followed by oxygen limitation | |||
Glycerol | 0.088 | 33.5c | ||||||||
Acetate | 0.006a | 2.3 | ||||||||
[36] | ✓ | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.462 | 108.6 | Glucose, YP medium, fed-batch, bioreactor, full aeration followed by oxygen limitation | ||
Acetoin | 0.02a | 4.6 | ||||||||
Acetate | 0.0004a | 0.1 | ||||||||
[27] | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.27 | 81.0 | Glucose, synthetic defined medium, fed-batch, flask, mild aerobic | |||
Glycerol | 0.239a | 71.8 | ||||||||
Succinate | 0.013a | 4.0 | ||||||||
[72] | ✓ | ✓ | n-Butanol | 0.012 | 0.130 | Glucose + pantothenate, SMD medium, flask, semi-anaerobic | ||||
Ethanol | 0.10 | ~1c | ||||||||
Glycerol | 0.17 | ~2c | ||||||||
[43] | ✓ | ✓ | ✓ | Isobutanol | 0.0074a | b | Glucose, SMG medium + Tween-80 + ergosterol, batch, serum bottle, microaerobic | |||
Ethanol | 0.033a | b | ||||||||
Glycerol | 0.26a | b | ||||||||
Pyruvate | 0.02a | b | ||||||||
2,3-butanediol | 0.325a | b | ||||||||
Dihydroxyisovalerate | 0.05a | b | ||||||||
Isobutyrate | 0.03a | b | ||||||||
[61] | ✓ | ✓ | Isobutanol | 0.0535 | 8.49 | Glucose, SC-Ura, fed-batch, bioreactor, microaerobic | ||||
2-Methyl-1-butanol | 0.01417 | 2.38 | ||||||||
Ethanol | 0.187 | 39.8 | ||||||||
Glycerol | b | b | ||||||||
[28] | ✓ | ✓ | ✓ | ✓ | Free fatty acids | 0.1 | 25 | Glucose, minimal N₂-limited medium, fed-batch, bioreactor, aerobic | ||
Glycerol | b | b | ||||||||
[42] | ✓ | ✓ | ✓ | Malic acid | 0.31a | 59 | Glucose, synthetic medium, batch, flask, aerobic | |||
Succinate | 0.04a | 8 | ||||||||
Glycerol | 0.13a | 25 | ||||||||
Pyruvate | 0.02a | 3 | ||||||||
Fumarate | 0.01a | 2 | ||||||||
[54] | ✓ | ✓ | ✓ | Succinic acid | 0.044a | 2.2 | Glucose + formate, mineral salt medium, deep-well plate, microaerobic | |||
Pyruvate | 0.364a | 18.2 | ||||||||
Malate | 0.022a | 1.1 | ||||||||
Glycerol | 0.076a | 3.8 | ||||||||
[60] | ✓ | ✓ | Gluconate | b | 2.31 | Glucose, synthetic defined, batch, culture tube, semi-anaerobic | ||||
Ethanol | b | 1.01 | ||||||||
Glycerol | b | b | ||||||||
[41] | ✓ | ✓ | Lactic acid | 0.6 | 80 | Glucose, YP medium, fed-batch, bioreactor, aerobic | ||||
Ethanol | 0.01 | 1.6 | ||||||||
Glycerol | 0.02 | 2.6 | ||||||||
[40] | ✓ | Lactic acid | 0.8 | 112.0 | Glucose, YP medium, fed-batch, flask, aerobic | |||||
Ethanol | 0.02a | 2.6 | ||||||||
[69] | ✓ | ✓ | ✓ | Lactic acid | 0.43a | 7.8 | 2-stage sugar consumption (ethanol then xylose), YP medium, batch, bioreactor, aerobic followed by microaerophilic | |||
Acetate | 0.16a | 3c | ||||||||
Xylitol | 0.01a | 0.17c | ||||||||
[70] | ✓ | ✓ | Lactic acid | 0.67 | 60 | Xylose, YP medium, batch, flask, aerobic | ||||
Ethanol | 0.01a | <1 | ||||||||
Xylitol | 0.01a | <1 | ||||||||
Glycerol | 0.01a | <1 | ||||||||
Acetate | 0.01a | <1 | ||||||||
[68] | ✓ | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.46a | 96.8 | Xylose + glucose, YP medium, fed-batch, bioreactor, microaerobic | ||
Glycerol | 0.11a | 23.3 | ||||||||
Ethanol | 0.08a | 16.3 | ||||||||
Xylitol | 0.03a | 5.9 | ||||||||
[73] | ✓ | ✓ | ✓ | 2,3-Butanediol | 0.26a | 43.6 | Xylose + glucose, YP medium, fed-batch, bioreactor, microaerobic | |||
Glycerol | 0.26a | 45 | ||||||||
Xylitol | 0.03a | 4.7 | ||||||||
[63] | ✓ | ✓ | Isobutanol | 0.026a | 2.6 | Xylose, nutrient-rich Verduyn medium, fed-batch, bioreactor, aerobic | ||||
Ethanol | 0.275a | ~27.5c | ||||||||
Glycerol | 0.10a | ~10 g/Lc | ||||||||
[62] | ✓ | ✓ | Isobutanol | 0.0196 | 3.10 | Xylose, synthetic medium, fed-batch, conical tube, semi-anaerobic | ||||
2-Methyl-1-butanol | 0.0053 | 0.79 | ||||||||
Ethanol | 0.32a | <50c | ||||||||
Glycerol | b | b | ||||||||
[67] | ✓ | ✓ | 1,2-Propanediol | 0.129 | 4.3 | Glycerol, YP medium, batch, bioreactor, aerobic | ||||
Ethanol | ~0a | ~0c |
Bold = product of interest
Italics = by-product
Absence of ethanol or glycerol in a row indicates it was not detected or that the yield or titer was <0.01
Yield not directly reported. Yield is either read from a graph, converted from a molar yield, calculated as g/g consumed carbon source, or calculated by dividing production rate by carbon source uptake rate.
Not reported
Titer not directly reported. Titer is either read from a graph, converted from molar concentration, or calculated as g/L fed carbon source, which is quantified by multiplying the reported yield (g/g carbon source) by the carbon source concentration (g/L).