Research Article
Carbon Dioxide Absorption Modeling for Off-Gas Treatment in the Nuclear Fuel Cycle
Table 3
Information used in solving the proposed reaction model.
| | Equation no. (reaction) | Forward rate (kfi) | Equilibrium constant | Reverse rate (kri) |
| | (B.1) (9) | k1f = exp(24.4 − 6864/Tl) (Reference [22]) | K1 = K2/(K5K6) (Reference [2]) | k1r = (k1f)/K1 | | (B.2) (10) | kf2 = 0.024 (Reference [28]) | K2 = 1E6exp(231.465 − 12092.1/Tl − 36.782ln(Tl)) (Reference [29]) | k2r = (k2f)/K2 | | (B.3) (11) | k3f = exp[31.396 − 6658/Tl]1E−3 (Reference [23]) | K3 = exp(31.396 − 6658/Tl)/1000 (Reference [2]) | k3r = (k3f)/K3 | | (B.4) (12) | k4f = 2E − 5 (Reference [30]) | K4 = 9.234E19exp(0.0772Tl) (Reference [29]) | k4r = (k4f)/K4 | | (B.5) (13) | k5f = 0.1 (Reference [2]) | K5 = 1E6exp(0.8−8094.8/Tl − 0.00748Tl) (Reference [29]) | k5r = (k5f)/K5 | | (B.6) (14) | k6f = 0.1 (Reference [2]) | K6 = 2E5exp(1.283 − 3456.2/Tl) (Reference [29]) | k6r = (k6f)/K6 | | (B.7) (5) | k7f = 2.5E − 3 exp(23.17 − 6894.8/Tl) (Reference [12]) | K7 = K2/K9 (Reference [12]) | k7r = (k7f)/K7 | | (B.8) (16) | K8f = 0.1 (Reference [19]) | K8 = 1E6exp(0.8 − 8094.8/Tl − 0.00748Tl) (Reference [29]) | k8r = (k8f)/K8 |
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