Research Article
Carbon Dioxide Absorption Modeling for Off-Gas Treatment in the Nuclear Fuel Cycle
Table 4
Typical values of column geometric parameters and operating variables.
| Parameter | Unit | Default value | Range | Reference |
| Height | M | 5 | 1–10 | Richardson et al. [37] | Tower diameter | M | 1 | 0.5–2 | Richardson et al. [37] | Dry specific area (aT) | m2/m3 | 200 | 200–500 | Billet and Schultes [38] | Void fraction (ε) | m3/m3 | 0.979 | 0.979 | Billet and Schultes [38] | Packing equivalent diameter | M | 0.01 | 0.005–0.02 | Billet and Schultes [38] | Packing coefficient (Cl) | Dimensionless | 0.971 | 0.971 | Billet and Schultes [38] | Packing coefficient (Ch) | Dimensionless | 0.547 | 0.547 | Billet and Schultes [38] | Packing coefficient (Cv) | Dimensionless | 0.390 | 0.390 | Billet and Schultes [38] | Liquid-phase superficial velocity (ul) | m/s | 0.01 | 0.001–0.1 | Greer [2] | Gas-phase superficial velocity (ug) | m/s | 1 | 0.5–5 | Greer [2] | Input temperature | K | 313 | 293–323 | Greer [2] | CO2 concentration | mol/m3 | 1.7 | 0.017–17.0 | This work | RNH2 molar fraction | Dimensionless | 0.2 | 0.01–0.5 | Greer [2] | R1R2R3N molar fraction | Dimensionless | 0.1 | 0.01–0.2 | This work |
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