Table 6.
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 |
YCit/S: g of citric acid produced per gram of carbon substrate consumed (maximum values).
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.
D = 0.009 h–1.
Strain JMY1203 is genetically engineered strain derivative from W29, with inactivated 2‐methyl‐citrate dehydratase.
Strain PR32 is genetically engineered strain derivative from SWJ‐1b, with over‐expressed pyruvate carboxylase.