Table 3 Proposed parameters based on the thermal data for the two carbonate loss substeps
Sample number | Substep c(1) | Substep c(2) | c(1)/c(2) | c(2)/c(1) | c(1) + c(2) |
|---|---|---|---|---|---|
1 | 1.5 | 0.4 | 3.75 | 0.267 | 1.9 |
2 | 1.7 | 0.3 | 5.67 | 0.176 | 2.0 |
3 | 1.4 | 0.3 | 4.67 | 0.214 | 1.7 |
4 | 1.6 | 0.4 | 4.00 | 0.250 | 2.0 |
5 | 1.5 | 0.0 | ∞ | 0.000 | 1.5 |
6 | 1.1 | 0.0 | ∞ | 0.000 | 1.1 |
7 | 1.4 | 0.0 | ∞ | 0.000 | 1.4 |
8 | 1.5 | 0.4 | 3.75 | 0.267 | 1.9 |
9 | 1.4 | 0.0 | ∞ | 0.000 | 1.4 |
10 | 1.6 | 0.4 | 4.00 | 0.250 | 2.0 |
11 | 2.0 | 0.0 | ∞ | 0.000 | 2.0 |
12 | 2.6 | 1.0 | 2.60 | 0.385 | 3.6 |
13 | 2.1 | 0.0 | ∞ | 0.000 | 2.1 |
14 | 0.0 | 1.5 | 0.00 | ∞ | 1.5 |
15 | 3.1 | 0.8 | 3.87 | 0.258 | 3.9 |
16 | 3.5 | 1.2 | 2.92 | 0.343 | 4.7 |
17 | 3.5 | 1.0 | 3.50 | 0.286 | 4.5 |
18 | 3.0 | 0.8 | 3.75 | 0.267 | 3.8 |
19 | 3.3 | 0.8 | 4.12 | 0.242 | 4.1 |
20 | 2.8 | 0.0 | ∞ | 0.000 | 2.8 |
21 | 2.7 | 0.4 | 6.75 | 0.148 | 3.1 |
22 | 3.6 | 1.5 | 2.40 | 0.417 | 5.1 |
23 | 2.7 | 0.9 | 3.00 | 0.333 | 3.6 |