Used 2,600 Nm3/hr (95,000 SCFH) 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.