| |
T (°K) |
|
|
|
|
|
| Flow Mole Ratio |
1023K |
1073K |
1103K |
973K |
1023K |
1103K |
| CH4 |
0.612 |
0.612 |
0.612 |
0.699 |
0.699 |
0.699 |
| O2 |
0.051 |
0.051 |
0.051 |
0.095 |
0.095 |
0.095 |
| N2 |
0.337 |
0.337 |
0.337 |
0.206 |
0.206 |
0.206 |
| CH4 Conversion (%) |
|
|
|
|
|
|
| Experimental[39] |
4.9 |
7.9 |
9.9 |
4.1 |
7.1 |
14.4 |
| Simulated[38] |
4.9 |
8.5 |
10.9 |
3 |
5.8 |
13.7 |
| Present work |
6.5 |
8.9 |
11.8 |
7.7 |
9 |
13.76 |
| C2 selectivity (%) |
|
|
|
|
|
|
| Experimental[39] |
55.6 |
69.2 |
72.5 |
35.6 |
53.7 |
69.6 |
| Simulated[38] |
54.6 |
64.5 |
66.4 |
31.7 |
46.4 |
58.9 |
| Present work |
56.5 |
60 |
56 |
33.46 |
46 |
51 |
| C2 Yield (%) |
|
|
|
|
|
|
| Experimental[39] |
2.7 |
5.5 |
7.2 |
1.5 |
3.8 |
10 |
| Simulated[38] |
2.7 |
5.5 |
7.3 |
1.0 |
2.7 |
8.1 |
| Present work |
3.8 |
5.35 |
6.7 |
2.6 |
4.1 |
6.9 |
|
