Strains | Substrate | Methods | Productivity/Yield | Reference |
---|---|---|---|---|
1,3-Propanediol | Â | Â | Â | Â |
Lactobacillus reuteriATCC 23272 | Glucose and glycerol | Co-fermentation | 1 g/l/h | [62] |
Lactobacillus panis PM1 | Glycerol or/and Glucose | - | - | [34] |
Klebsiella pneumoniae J2B | Glycerol | Fed-batch fermentation | 0.15 g/l/h | [30] |
Klebsiella pneumoniae CGMCC 2028 | Glycerol | Continuous fermentation | 0.43 g/g | [63] |
Citrobacter freundii DSM 15979 | Crude glycerol | Packed bed biofilm reactors operating under continuous conditions | - | [64] |
Pantoeaagglomerans DSM 30077 | Â | Packed bed biofilm reactors operating under continuous conditions | 4 g/l/h PUF* | [64] |
Citrobacteramalonaticus Y19 | Glycerol | anaerobic conditions using fumatate and CoCl2 as electron acceptors | 0.20 g/g | [28] |
Citrobacterfreundii FMCC-B 294(VK-19) | waste glycerol | Fed-batch fermentation | 0.79 g/l/h | [27] |
Clostridium butyricum VPI 3266 | Glycerol | Continuous cultures | - | [65] |
Clostridium butyricum VPI 1718 | Glycerol | Batch and continuous cultures | 0.56 g/g (batch culture) | [66] |
0.57 g/g (continuous culture) | ||||
Clostridium butyricum F2b | Industrial glycerol | Batch and continuous cultures | 6 g/ l/h (max) | [67] |
Clostridium saccharobutylicum NRRL B-643 | Glycerol | - | 0.30 g/g | [29] |
Clostridium beijerinckii NRRL B-593 | Raw glycerol | Immobilized bioreactor continuous operation | 0.78 g/g (ceramic rings) | [68] |
0.79 g/g (pumice stones) | ||||
2,3-Butanediol | Â | Â | Â | Â |
Paenibacilluspolymyxa | Raw inulin extract from Jerusalemartichoke tuber | Batch fermentation | 0.88 g/l/h | [23] |
2,4-Pentanediol | Â | Â | Â | Â |
Candida boidinii KK912 | 2,4-Pentanedione | - | - | [69] |