From: Continuous succinic acid production by Actinobacillus succinogenes on xylose-enriched hydrolysate
Substrate (feedstock) | Pretreatment method | Mode | q SA (g L−1 h−1)a | C SA (g L−1)b | Y sSA (g g−1)c | References |
---|---|---|---|---|---|---|
Corn stover (xylose, glucose, arabinose, galactose) | Pilot scale: deacetylation followed by dilute sulphuric acid hydrolysis | Continuous | 1.77 | 39.6 | 0.78 | This study |
Xylose | – | Continuous | 2.64 | 32.5 | 0.77 | This study |
Xylose | – | Continuous | 3.41 | 29.4 | 0.68 | [46] |
Xylose (60 g L−1) | – | Batch | 0.94 | 38.4 | 0.70 | [37] |
Corn stover | Pilot scale: deacetylation followed by dilute sulphuric acid hydrolysis (DDAP-H) | 0.30 | 42.8 | 0.74 | ||
Pilot scale: dilute sulphuric acid hydrolysis (DAP-H) | 0.12 | 17.0 | 0.52 | |||
Mock DDAP-H (xylose, glucose, arabinose, galactose, inhibitors, low acetate) | – | 0.61 | 43.8 | 0.68 | ||
Mock DAP-H (xylose, glucose, arabinose, galactose, inhibitors, high acetate) | – | 0.61 | 43.7 | 0.72 | ||
Sugarcane bagasse (xylose) | Dilute sulphuric acid hydrolysis | Batch | 1.01 | 22.5 | 0.43 | [57] |
Wheat (glucose) | Enzymatic hydrolysis | Batch | 1.01 | 35.6 | 0.82 | [58] |
1.57 | 64.2 | 0.81 | [59] | |||
0.91 | 62.1 | 1.02 | [60] | |||
Corn fibre (glucose, xylose, arabinose) | Dilute sulphuric acid hydrolysis by autoclaving | Batch | 0.98 | 35.4 | 0.73 | [61] |
0.63 | 47.0 | 0.68 | [62] | |||
Corn stover (glucose, xylose, arabinose) | Dilute sulphuric acid hydrolysis followed by cellulose treatment | Batch | 1.08 | 56.4 | 0.73 | [30] |
Sugarcane molasses (sucrose, glucose, fructose) | Sulphuric acid treatment of crude molasses | Batch | 1.30 | 60.7 | 0.81 | [63] |
Fed-batch | 1.40 | 64.7 | 0.86 | |||
Batch | 0.97 | 57.9 | 0.69 | [64] | ||
Fed-batch | 1.07 | 64.3 | 0.76 | |||
Glucosed | – | Continuous | 10.8 | 32.5 | 0.90 | [12] |
– | Fed-batch | 2.77 | 98.7 | 0.89 | [65] |