Page 170 - Entrophy Analysis in Thermal Engineering Systems
P. 170

Entropy and chemical equilibrium                             165


                 A comparison between the measured and predicted molar contents of
              carbon dioxide and carbon monoxide plotted against the air ratio is displayed
              in Fig. 10.7. The measured data are shown with symbols. The dashed lines
              represent the prediction of the traditional equilibrium model based on Gibbs
              function minimization. The solid lines denote the predictions of the mod-
              ified model, which takes into account the actual conversion of carbon
              through Eq. (10.29). Also, the air ratio is defined as the ratio of the actual
              air flow to the stochiometric air required for complete combustion.
              Fig. 10.8 depicts a comparison between the predictions of the two models
              and the experiments for hydrogen and methane concentrations.
                 The modified model successfully captures the experimentally measured
              molar contents of CO, CO 2 , and H 2 . However, its prediction of CH 4
              content is significantly lower than the measured data. The authors attributed
              the large concentration of methane to the pyrolysis reactions and quoted that
              the char gasification may be achieved to a limited extent in a pilot-scale
              gasifier. Furthermore, the heating value of the syngas computed by the
              traditional equilibrium model is reported to be substantially higher than
              the experiments, whereas the modified model predictions are in a good
              agreement with the measured values of the heating value.



                           100
                                                       Measured CO
                                                       Measured CO 2
                                      CO eq.
                           Molar content (%)  10  CO 2  eq.  CO  fit
                                                  2
                                                CO fit








                             1
                             0.3  0.35   0.4  0.45  0.5   0.55  0.6
                                            Air ratio (−)
              Fig. 10.7 Comparison of the measured and predicted CO and CO 2 contents using the
              traditional equilibrium model (dashed lines) and the modified model (solid lines) at var-
              ious air ratios. Data are obtained for Highvale coal gasified at 1100K and 155kPa. (From
              X. Li, J.R. Grace, A.P. Watkinson, C.J. Lim, A. Erg€ udenler, Equilibrium modeling of gasification:
              a free energy minimization approach and its application to a circulating fluidized bed coal
              gasifier, Fuel 80 (2001) 195–207.)
   165   166   167   168   169   170   171   172   173   174   175