Used 95,000 SCFH (2,600 Nm3/hr) hydrogen plant.
Built in 1992.
Designed by Howe Baker Engineering of USA.
Product purity: 99.9%.
Feedstock: Natural Gas.
Inlet pressure approximately 50 PSIG.
Compressed to approximately 370 PSIG at 190 degrees F.
Feed gas stream is preheated to approximately 750 degrees F.
Uses cobalt-moly hydrotreating catalyst.
Desulfurizers and zinc oxide catalyst.
Superheated to 950 F in the reformer convection section reformer feed preheat coil.
Syngas reforming at a temperature of approximately 1440 degrees F.
Flue gas from the reformer at approximately 1900 degrees F.