Research Article
Thermochemical Equilibrium Model of Synthetic Natural Gas Production from Coal Gasification Using Aspen Plus
Table 4
Reactors temperature and pressure conditions, inlet streams, and other model facilities described in the Aspen Plus models.
| Facility or inlet stream | Temperature (°C) | Pressure (bar) |
| Coal stream | 27 | 1 | Water stream | 40 | 5 | Oxygen stream | 40 | 74.1 | CO2 stream | 100 | 83 | Steam stream | 250* | 49* |
| Reactor RGIBB-1 (Figure 5) | Bijao coal: 1658** Sanoha coal: 1413** | 50 | Reactor RGIBB-2 (Figure 5) | Bijao coal: 940** Sanoha coal: 922** | 50 | Reactor RGIBB-1 (Figure 6) | Bijao coal: 1340** Sanoha coal: 1508** | 50 | Reactor REQUIL-1 (Figure 7) | 250* (Bijao and Sanoha coals) | 49* | Reactor REQUIL-2 (Figure 9) | 350* (Bijao and Sanoha coals) | 42* |
| Heater HEATER-1 (Figure 5) | 202 | Isobaric | Heater HEATER-1 (Figure 6) | 167 | Isobaric | Heater HEATER-2 (Figure 7) | 40 | Isobaric | Heater HEATER-3 (Figure 9) | 54.7 | Isobaric |
|
|
*Adapted from [25]. **Simulation results.
|