Table 3.
No. | Time agitation process-static process | Tube volume (mL) | TUDCA (g/L) | T-7-KLCA (g/L) | TCDCA (g/L) | Ratio of TUDCA to TCDCA | TUDCA conversion efficiency (%) |
---|---|---|---|---|---|---|---|
1 | 0 h–0 h | ▲ | 0.00 | 0.00 | 1.10 | 0.00 | 0.00 |
2 | 3.5 h–0 h | ▲ | 0.04 | 0.00 | 1.06 | 0.04 | 3.55 |
3 | 6.5 h–0 h | ▲ | 0.07 | 0.01 | 1.00 | 0.07 | 6.05 |
4 | 16.5 h–0 h | ▲ | 0.18 | 0.04 | 0.89 | 0.20 | 15.94 |
5 | 0 h–16.5 h | 2 | 0.15 | 0.02 | 0.93 | 0.16 | 13.23 |
6 | 15 | 0.27 | 0.04 | 0.79 | 0.34 | 24.24 | |
7 | 50 | 0.26 | 0.01 | 0.83 | 0.31 | 23.30 | |
8 | 0 h–22 h | 2 | 0.19 | 0.05 | 0.86 | 0.22 | 17.22 |
9 | 15 | 0.30 | 0.03 | 0.78 | 0.40 | 27.73 | |
10 | 50 | 0.28 | 0.06 | 0.76 | 0.36 | 25.21 | |
11 | 0 h–48 h | 2 | 0.19 | 0.05 | 0.86 | 0.22 | 17.01 |
12 | 15 | 0.30 | 0.06 | 0.74 | 0.41 | 27.22 | |
13 | 50 | 0.21 | 0.16 | 0.73 | 0.28 | 18.92 | |
14 | 3.5 h–13 h | 2 | 0.54 | 0.03 | 0.52 | 1.05 | 49.58 |
15 | 15 | 0.56 | 0.04 | 0.50 | 1.11 | 50.76 | |
16 | 50 | 0.58 | 0.04 | 0.48 | 1.20 | 52.70 | |
17 | 3.5 h–18.5 h | 2 | 0.54 | 0.06 | 0.49 | 1.10 | 49.49 |
18 | 15 | 0.53 | 0.07 | 0.50 | 1.05 | 47.94 | |
19 | 50 | 0.52 | 0.07 | 0.51 | 1.02 | 47.10 | |
20 | 3.5 h–44.5 h | 2 | 0.50 | 0.09 | 0.51 | 0.98 | 45.52 |
21 | 15 | 0.51 | 0.09 | 0.50 | 1.02 | 46.42 | |
22 | 50 | 0.51 | 0.10 | 0.49 | 1.05 | 46.60 | |
23 | 6.5 h–10 h | 2 | 0.52 | 0.07 | 0.51 | 1.02 | 47.41 |
24 | 15 | 0.51 | 0.06 | 0.52 | 0.98 | 46.74 | |
25 | 50 | 0.52 | 0.06 | 0.52 | 1.00 | 47.20 | |
26 | 6.5 h–15.5 h | 2 | 0.42 | 0.07 | 0.61 | 0.69 | 38.25 |
27 | 15 | 0.41 | 0.08 | 0.61 | 0.67 | 37.36 | |
28 | 50 | 0.43 | 0.06 | 0.60 | 0.71 | 39.25 | |
29 | 6.5 h–41.5 h | 2 | 0.50 | 0.09 | 0.51 | 0.96 | 45.19 |
30 | 15 | 0.49 | 0.09 | 0.52 | 0.94 | 44.38 | |
31 | 50 | 0.51 | 0.09 | 0.50 | 1.03 | 46.66 | |
32 | 16.5 h–5.5 h | 2 | 0.19 | 0.06 | 0.85 | 0.22 | 17.25 |
33 | 15 | 0.20 | 0.07 | 0.83 | 0.24 | 17.83 | |
34 | 50 | 0.24 | 0.09 | 0.76 | 0.32 | 22.28 | |
35 | 16.5 h–31.5 h | 2 | 0.22 | 0.09 | 0.80 | 0.27 | 19.62 |
36 | 15 | 0.32 | 0.09 | 0.69 | 0.47 | 29.21 | |
37 | 50 | 0.32 | 0.09 | 0.69 | 0.46 | 28.94 |
▲These samples were directly taken from fermenters without static process. TUDCA conversion efficiency above 45.00% was highlighted in italics