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. 2017 Mar 13;17(6):695–709. doi: 10.1002/elsc.201600225

Table 6.

Experimental results of citric acid‐producing yeasts during growth under various fermentation configurations and comparisons with the present investigation

Strain Substrate Culture mode Cit (g/L) YCit/S a (g/g) Reference
Yarrowia lipolytica LGAM S (7) OMW/glycerol blend Shake flasks 30.3 0.62 Dourou et al. 9
Yarrowia lipolytica ACA‐DC 50109 OMW/glucose blend Shake flasks 28.9 0.53b Papanikolaou et al. 21
Yarrowia lipolytica W29 OMW/glucose blend Shake flasks 15.8 0.46b Sarris et al. 22
Yarrowia lipolytica ATCC 20346 Glucose Fed‐batch culture, bioreactor 50.0–69.0 0.52 Moresi 26
Yarrowia lipolytica JMY1203d Crude glycerol Shake flasks 57.7 0.92 Papanikolaou et al. 27
Yarrowia lipolytica LGAM S(7)1 Crude glycerol Shake flasks 35.1 0.44 Papanikolaou et al. 31
Candida oleophila ATCC 20177 Glucose Batch culture, flasks, bioreactor 50.1–79.1 0.55 Anastassiadis et al. 33
Yarrowia lipolytica N1 Ethanol Fed‐batch culture, bioreactor 120.0 0.85 Kamzolova et al. 41
Yarrowia lipolytica 187/1 Rapeseed oil Fed‐batch culture, bioreactor 135.1 1.55 Kamzolova et al. 42
Yarrowia lipolytica N15 Pure glycerol Fed‐batch bioreactor 98.0 0.70 Kamzolova et al. 43
Candida oleophila ATCC 20177 Glucose Continuous culture bioreactor 37.6–57.8 0.40 Anastassiadis and Rehm 45
Yarrowia lipolytica SWJ‐1b Glucose Batch bioreactor 52.3 0.87 Liu et al. 46
Candida lipolytica Y1095 Glucose Fed‐batch culture bioreactor 13.6–78.5 0.79 Rane and Sims 47
Yarrowia lipolytica Wratislavia 1.31 Crude glycerol Batch bioreactor 124.5 0.62 Rymowicz et al. 49
Yarrowia lipolytica A‐101‐1.22 Crude glycerol Batch bioreactor 112.0 0.60 Rymowicz et al. 50
Yarrowia lipolytica Wratislavia AWG7 Crude glycerol Repeated batch 154.0 0.78 Rywińska and Rymowicz 51
Yarrowia lipolytica NG40/UV7 Pure glycerol Fed‐batch bioreactor 115.0 0.64 Morgunov et al. 53
Candida lipolytica NRRL Y‐1095 n‐Paraffins Fed‐batch culture bioreactor 30.0–40.0 1.00 Crolla and Kennedy 54
Saccharomycopsis lipolytica D 1805 Glucose Batch culture, bioreactor 95.0 0.75 Briffaud and Engasser 55
Saccharomycopsis lipolytica NRRL Y‐7576 Glucose Batch culture, bioreactor 51.5 0.71 Klasson et al. 56
Candida guillermondii IMK 1 Galactose Shake flasks 13.5 0.38 Gutierrez et al. 57
Candida lipolytica Y 1095 Glucose Continuous culture recycling, bioreactor 40.0–50.0 0.72 Rane and Sims 58
Yarrowia lipolytica ACA‐DC 50109 Commercial glucose Shake flasks 42.9 0.56 Papanikolaou et al. 59
Yarrowia lipolytica AWG‐7 Glucose syrup Shake flasks 36.7 0.31 Rymowicz and Cibis 60
Yarrowia lipolytica NRRL YB‐423 Pure glycerol Shake flasks 21.6 0.55 Levinson et al. 61
Yarrowia lipolytica LFMB 20 Crude glycerol Shake flasks 42.0 0.39 Papanikolaou et al. 62
Commercial glucose 58.1 0.55
Yarrowia lipolytica A‐101 Crude glycerol Batch bioreactor 66.8 0.43 Rywińska et al. 63
Yarrowia lipolytica Wratislavia 1.31 Crude glycerol Fed‐batch bioreactor 126.0 0.63 Rywińska et al. 64
157.5 0.58
Yarrowia lipolytica Wratislavia AWG7 Pure glycerol Continuous bioreactorc 86.5 0.59 Rywińska et al.65
Yarrowia lipolytica PR32e Glucose Fed‐batch bioreactor 111.1 0.93 Fu et al.66
Yarrowia lipolytica ACA‐YC 5033 OMW/glucose blend Shake flasks 52.0 0.64b Present study
a

YCit/S: g of citric acid produced per gram of carbon substrate consumed (maximum values).

b

In the case of OMW/glucose blends, the conversion yield was based on the reducing sugars (OMWs contained some quantities of reducing sugars) consumed by the strains.

c

D = 0.009 h–1.

d

Strain JMY1203 is genetically engineered strain derivative from W29, with inactivated 2‐methyl‐citrate dehydratase.

e

Strain PR32 is genetically engineered strain derivative from SWJ‐1b, with over‐expressed pyruvate carboxylase.