Table 2 Design matrix using CCD and bio-oil yield.
Experimental run | A: Pyrolysis temp (°C) | B: Vapour cooling temp (°C) | C: Residence time (min) | D: Gas flow rate (l min−1) | Bio-oil yield (%) |
|---|---|---|---|---|---|
1 | 300 | 2 | 15 | 3 | 9.2 |
2 | 400 | 6 | 25 | 1 | 16 |
3 | 300 | 6 | 25 | 2 | 13 |
4 | 500 | 10 | 15 | 1 | 14.5 |
5 | 400 | 6 | 25 | 2 | 17.2 |
6 | 500 | 2 | 35 | 3 | 15.5 |
7 | 500 | 6 | 25 | 2 | 15.7 |
8 | 300 | 10 | 35 | 3 | 8.1 |
9 | 300 | 2 | 15 | 1 | 13.5 |
10 | 500 | 2 | 35 | 1 | 17.2 |
11 | 500 | 2 | 15 | 3 | 14.8 |
12 | 300 | 10 | 15 | 1 | 7.8 |
13 | 400 | 6 | 25 | 2 | 17.9 |
14 | 500 | 10 | 35 | 3 | 10.9 |
15 | 400 | 6 | 15 | 2 | 16.7 |
16 | 300 | 10 | 15 | 3 | 7.7 |
17 | 400 | 10 | 25 | 2 | 13.6 |
18 | 300 | 2 | 35 | 3 | 14.5 |
19 | 400 | 2 | 25 | 2 | 17.8 |
20 | 300 | 2 | 35 | 1 | 15.5 |
21 | 300 | 10 | 35 | 1 | 8.9 |
22 | 400 | 6 | 25 | 3 | 13.8 |
23 | 400 | 6 | 25 | 2 | 17.1 |
24 | 400 | 6 | 25 | 2 | 17.6 |
25 | 500 | 2 | 15 | 1 | 16.7 |
26 | 400 | 6 | 25 | 2 | 16.7 |
27 | 500 | 10 | 15 | 3 | 12.8 |
28 | 400 | 6 | 35 | 2 | 18.9 |
29 | 500 | 10 | 35 | 1 | 13.8 |
30 | 400 | 6 | 25 | 2 | 17.5 |