Table 3.
Comparison of L-MA production from various LB by microorganisms.
| Substrate | Pretreatment | Substrate concentration | Microorganism | Process mode | L-MA (g/l) | Yield (g/g) | Productivity (g/l/h) | Reference |
|---|---|---|---|---|---|---|---|---|
| Corn hull hydrolysate | Non- pretreatment (Milled into small particles) | 100 g/l (88 g/l xylose) | A. tropicalis H1 | 15-ml shake flask, batch, 120 h, 37ºC | 77.09 | 0.77 | 0.64 | This study |
| Xylose | - | 100 g/l | A. tropicalis H1 | 15-ml shake flask, batch, 120 h, 37ºC | 87.53 | 0.88 | 0.73 | This study |
| Milled corn stover | Non-pretreatment (Milled into small particles) | 50 g/l | Thermobifida fusca muC-16 | 3-l bioreactor, batch (120 h), 55ºC | 21.47 | 0.43 | 0.18 | [10] |
| Barley straw | Acid | 95 g/l (56 g/l glucose, 33 g/l xylose and 6 g/l arabinose) | Aureobasidium pullulans Y-2311-1 | 125-ml shake flask, batch (288 h), 25ºC | 43.54 | 0.30 | 0.48 | [34] |
| Beech wood hemicellulose hydrolysate | Organosolv | 99.5 g/l | Aspergillus oryzae DSM 1863 | 2-l bioreactor, batch (168 h), 32ºC | 5.8 | - | 0.03 | [30] |
| Corncob hydrolysate | Acid | 150 g/l (96 g/l glucose and 54 g/l xylose) A. pullulans CCTCC M2012223 | 5-l bioreactor, batch (864 h), 25ºC | 38.6 | 0.30 | 0.40 | [43] | |
| Corn fiber hydrolysate | Chemical (alkaline + H2O2) | 50 g/l | A. pullulans NRRL 50383 | 50-ml shake flask, batch (168 h), 25ºC | 11.6 | - | 0.07 | [44] |
| Corn straw hydrolysate | Stream-steam-explosion jar and dilute acid | 125 g/l (100 g glucose and 25 g xylose) | Rhizopus delemar HF-121 | 3-l bioreactor, batch (60 h), 30ºC | 120.5 | 0.96 | 2.01 | [37] |
| Wheat straw hydrolysate | Chemical (alkaline + H2O2) | 50 g/l | A. pullulans NRRL 50383 | 50-ml bioreactor, fed- batch (168 h), 25ºC | 27 | - | 0.16 | [44] |