Table 2. Kinetic Equations and the Relationship between Initial/Final Concentrations ([C]i/[C]f) of Reactant (S)/Product (SiS2) and Reaction Time (t).
| |||||||
---|---|---|---|---|---|---|---|
t = 0 | Conc. (mol/dm3) | a | b | c | 0 | ||
[C]i,1023 Ks–l | 1.23 | 0.880 | 0.302 | 0 | |||
[C]i,1023 Ks–g | 1.23 | 0.880 | 0.302 | 0 | |||
[C]i,1073 Ks–l | 1.23 | 0.680 | 0.429 | 0 | |||
[C]i,1073Ks–g | 1.23 | 0.680 | 0.429 | 0 |
t = t | Conc. (mol/dm3) | a – x | b – ux |
|
x | |
---|---|---|---|---|---|---|
[C]1023Ks–l | 1.23 – x | 0.880 – 2/3x | 0.302 | x | ||
[C]1023Ks–g | 1.23 – x | 0.880 – 2/3x | 0.302 | x | ||
[C]1073Ks–l | 1.23 – x | 0.680 – 2/3x | 0.429 | x | ||
[C]1073Ks–g | 1.23 – x | 0.680 – 2/3x | 0.429 | x |
t = ∞ | Conc. (mol/dm3) | 0 | bl,∞ | cg,∞ | a |
---|---|---|---|---|---|
[C]f, 1023Ks–l | 0 | 0.060 | 0.302 | 1.23 | |
[C]f,1023Ks–g | 0 | 0.060 | 0.302 | 1.23 | |
[C]f,1073Ks–l | 0 | 0.000 | 0.340 | 1.23 | |
[C]f,1073Ks–g | 0 | 0.000 | 0.340 | 1.23 |