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. Author manuscript; available in PMC: 2021 Dec 1.
Published in final edited form as: Curr Opin Chem Biol. 2020 Oct 5;59:182–192. doi: 10.1016/j.cbpa.2020.08.005

Table 1.

Summary of strategies for non-ethanol chemical production in S. cerevisiae

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

a =

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.

b =

Not reported

c =

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).