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. 2021 May 27;105(11):4467–4486. doi: 10.1007/s00253-021-11355-2

Table 1.

Overview on biotechnological erythritol production methods using conventional carbon sources

Substrate Microorganism Type of culture Substrate Erythritol production Biomass concentration By-products By-product to erythritol ratio % Cultivation medium Ref.
Initial Final g/Lb g/L.h g/gc g/Lb Compound g/Lb Main components of the cultivation medium Concentration range
g/Lb g/Lb g/Lb
Commercial glucose Candida magnoliae B 237 0 60.3 0.37 0.25 31.73 Mannitol 3.3 5.7 YE 0.23–9.2 Savergave et al. (2011)
KH2PO4
Glycerol 0.3 MgSO4·7H2O
B 200 N.R. 20.3 0.12 0.1 N.R. Glycerol 2.4 10.4 YE, 0.25–10 Ghezelbash et al. (2014)
KH2PO4
MgSO4
FB 250 N.R. 200 1.2 0.43 ±60 N.R. N.R. Peptone 2.0–20 Koh et al. (2003)
YE
Phytic acid
FB 250 0 87.8 0.61 0.35 38.4 No by-products YE 0.23–9.2 Savergave et al. (2011)
KH2PO4
MgSO4·7H2O
FB 400 N.R. 164 2.8 0.41 75 Glycerol 137a 83.5 YE 212 Ryu et al. (2000)
Citric acid
Butyric acid
Candida sorbosivorans B 160 N.R. 60.2 0.5 0.38 N.R. N.R. N.R. YE, 0.35–12 Saran et al. (2015)
KH2PO4
MgSO4·7H2O
FeSO4·7H2O
Pseudozyma tsukubaensis FB 400 0 241 2.84 0.6 22.8 No by-products MnSO4·4H2O 2.0–15 Jeya et al. (2009)
CuSO4·5H2O
Corn steep powder
Trichosporonoides oedocephalis B 200 0.5* 50.54 0.39 0.25 27.43 Glycerol 6.4 11.3 YE 0.5–10 Li et al. (2017)
KH2PO4
MgSO4,
KCl
B 300 5 59.34 0.49 0.2 35.1 Glycerol 30.9 34.2 YE 0.5–10 Kang et al. (2019)
KH2PO4
MgSO4,
NaCl
CuSO4·5H2O
Betaine
Commercial glycerol Yarrowia lipolytica C 300 0 199 0.8 0.66 20.6 Arabinitol 2.5 3.4 YE 0.22–26.5 Rakicka et al. (2017)
Mannitol 2.1 (NH4)2SO4
Citric acid 2 KH2PO4
α-ketoglutaric acid 0.3 MgSO4·7H2O NaCl
Commercial xylose Aurebasidium pullulans B 120 38.6 31.75 0.22 0.26 32.28 N.R. N.R. YE 0.35–17.82 Guo et al. (2016)
KH2PO4
Citric acid

YE yeast extract, N.R. not reported

aTotal organic acid

bPer litre of culture

cPer gram of carbon source