Table 3.
Comparison of lactic acid fermentation using sugarcane bagasse as raw material from several studies.
Microbial host | Strategies | Time (h) | Titer (g L−1) | Yield (g g−1 glucose) | Productivity (g L−1 h−1) |
---|---|---|---|---|---|
Bacillus coagulans DSM231438 (wild-type, bacteria) |
Pretreated using acid and steam explosion method Cell adaptation using furfural prior to fermentation Enzyme hydrolysis using Genencor GC220 Fermentation at 50 °C, 100 rpm (1-L reactor) Two-stage simultaneous saccharification and fermentation pH control at 5 using Ca(OH)2 at the beginning and during fermentation |
37 | 58.2 | 0.90 | 1.81 |
Lactobacillus pentosus39 (wild-type, bacteria) |
Pretreated using acid and steam explosion method Cell adaptation using hydrolysate prior to fermentation Enzyme hydrolysis using Cellic C-TEC2 Fermentation at 37 °C, 200 rpm (1-L bioreactor) Fed-batch simultaneous saccharification and fermentation pH control at 6–6.5 using NaOH at the beginning and during fermentation |
72 | 72.8 | 0.61 | 1.01 |
B. coagulans DSM ID 14-30040 (wild-type, bacteria) |
Pretreated using acid method Bio-detoxification treatment Fermentation at 52 °C, 200 rpm (500-mL reactor) pH control at 6.0 using NaOH at the beginning and during fermentation |
50 | 56.0 | 0.87 | 1.70 |
B. coagulans NCIM 564841 (wild-type, bacteria) |
Pretreated using alkali method and followed by washing process Enzyme hydrolysis using Cellic C-TEC2 Fermentation at 50 °C, 100 rpm pH control at 7.0 using NaOH during fermentation |
24 | 69.2 | 0.76 | 2.88 |
S. cerevisiae BTCC3 LA2 (recombinant, yeast) |
Pretreated using hot water No prior detoxification or enzyme hydrolysis processes Fermentation at 30 °C, 90 rpm, high-cell density cultivation (100 mL-flask) No supplementation of a neutralizing agent at any stage of fermentation |
15 | 25.34 | 0.51 | 1.69 |