9. Comparison of the Molar Flow of Components in the Output of Reactors for Industrial Data and Modeling.
| data |
kinetic model |
rel. deviation |
deviation % |
|||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| composition (kgmol/h) | R1 | R2 | R3 | R1 | R2 | R3 | R1 | R2 | R3 | R1 | R2 | R3 |
| H2S | 23.99 | 8.16 | 4.98 | 24.58 | 8.18 | 4.97 | –0.59 | –0.02 | 0.01 | –2.46 | –0.30 | 0.21 |
| SO2 | 10.77 | 2.86 | 1.27 | 11.08 | 2.86 | 1.28 | –0.31 | 0.00 | –0.01 | –2.88 | –0.16 | –0.86 |
| N2 | 552.37 | 552.37 | 552.37 | 552.37 | 552.37 | 552.39 | 0.00 | 0.00 | –0.02 | 0.00 | 0.00 | 0.00 |
| CO | 27.51 | 27.51 | 27.51 | 27.51 | 27.51 | 27.51 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 |
| CO2 | 337.18 | 337.18 | 337.18 | 337.16 | 337.18 | 337.18 | 0.02 | 0.00 | 0.00 | 0.01 | 0.00 | 0.00 |
| COS | 0.50 | 0.50 | 0.50 | 0.51 | 0.50 | 0.50 | –0.01 | 0.00 | 0.00 | –2.80 | 0.00 | 0.00 |
| S2 | 0.15 | 0.01 | 0.00 | 0.12 | 0.01 | 0.00 | 0.03 | 0.00 | 0.00 | 20.00 | 0.00 | 0.00 |
| S6 | 3.00 | 0.53 | 0.17 | 3.15 | 0.54 | 0.16 | –0.15 | –0.01 | 0.01 | –5.00 | –1.32 | 4.00 |
| S8 | 9.63 | 3.47 | 1.27 | 9.45 | 3.46 | 1.28 | 0.18 | 0.01 | –0.01 | 1.87 | 0.29 | –0.86 |
| H2O | 355.68 | 371.50 | 337.18 | 355.08 | 371.49 | 337.18 | 0.60 | 0.01 | 0.00 | 0.17 | 0.00 | 0.00 |
| H2 | 14.63 | 14.63 | 14.63 | 14.63 | 14.63 | 14.63 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 |
| CS2 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 | 0.00 |