10. Comparison of Output Flow Characteristics of Reactors for Industrial Data and Modeling.
| data |
kinetic model |
rel. deviation |
deviation % |
|||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| total stream properties | R1 | R2 | R3 | R1 | R2 | R3 | R1 | R2 | R3 | R1 | R2 | R3 |
| temperature (°C) | 299.23 | 226.86 | 203.45 | 308.20 | 226.60 | 204.50 | –8.97 | 0.26 | –1.05 | –3.00 | 0.11 | –0.52 |
| molar flow rate (kgmol/h) | 1335.42 | 1318.72 | 1277.06 | 1335.64 | 1318.73 | 1277.08 | –0.22 | –0.01 | –0.02 | –0.02 | 0.00 | 0.00 |
| molecular weight (kg/kgmol) | 31.54 | 29.79 | 29.29 | 31.72 | 31.72 | 31.72 | –0.18 | –1.93 | –2.43 | –0.57 | –6.48 | –8.30 |
| actual density (kg/m3) | 1.05 | 1.05 | 1.00 | 0.93 | 0.93 | 0.93 | 0.12 | 0.12 | 0.07 | 11.43 | 11.43 | 7.00 |
| viscosity (cP) | 0.02 | 0.02 | 0.02 | 0.02 | 0.02 | 0.02 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 |
| heat flow (MW) | –58.65 | –60.31 | –60.77 | –57.92 | –57.92 | –57.92 | –0.73 | –2.39 | –2.85 | 1.24 | 3.96 | 4.69 |
| molar enthalpy (kJ/kgmol) | –158,107.93 | –164,652.05 | –166,432.50 | –156,500.00 | –156,500.00 | –156,500.00 | –1607.93 | –8152.05 | –9932.50 | 1.02 | 4.95 | 5.97 |
| mass heat capacity (kJ/kg K) | 1.16 | 1.20 | 1.16 | 1.19 | 1.19 | 1.19 | –0.03 | 0.01 | –0.03 | –2.59 | 0.83 | –2.59 |
| thermal conductivity (W/m K) | 0.04 | 0.04 | 0.03 | 0.04 | 0.04 | 0.04 | 0.00 | 0.00 | –0.01 | 2.50 | 2.50 | –30.00 |