Table 3.
Utilized fuel module values for the investigation of the converter.
| Variable | Values |
|---|---|
| Fuel module functioning cells (N) | 65 |
| Fuel module functioning H2 pressure | 1.8976 bar |
| Fuel module functioning O2 pressure | 1.2032 bar |
| Inside fuel module air operating value (Ipm) | 505.321 |
| Inside fuel module operating gas value (R) | 86.2453 [J mol−1 K−1] |
| Applied Faraday value for the working polymer fuel module | 94,3245.108 [C mol−1] |
| Obtained polymer fuel module voltage at peak demand condition | 65.12 V |
| Obtained polymer fuel module power at peak demand condition | 5.9999 kW |
| Obtained polymer fuel module current at peak demand condition | 134 A |
| Evaluated openly available fuel module voltage | 65.213 V |
| Utilized oxygen content for the polymer fuel module operation | 62.8769% |
| Utilized hydrogen content for the polymer fuel module operation | 99.2185% |
| The entire oxidation value for the polymer fuel system operation | 99.1156% |
| Overall oxygen decomposition happened in the fuel system | 22.89712% |