8th International Hydrogen Technologies, Diyarbakır, Türkiye, 12 - 15 Mayıs 2024, ss.174-177
The catalytic thermal H2S decomposition reaction has recently
attracted intense attention from researchers for the production of COx-free H2.
In this study, tungsten oxide (W-O) and iron oxide (Fe-O) catalysts were
prepared by the complexation method. Catalytic activity tests of single metal
oxides were performed in a continuously flow packed-bed reactor system at 800
°C using a conventional heating system and 1% H2S-N2
mixture. Catalysts properties were determined using XRD, EDS and N2-Adsorption-desorption
technique. As a result of activity tests, 12% H2S and 4% H2S
conversions were obtained with W-O catalyst and Fe-O catalyst, respectively. At
the same temperature and gas composition, the thermodynamic equilibrium H2S
conversion is 28%. Activity test results performed in 60 minutes showed that
the W-O catalyst was more stable and had higher activity in obtaining H2
through H2S decomposition. Synthesis and characterization studies
continue within the scope of this study.
Keywords: Tungsten, Iron, H2
Production, H2S decomposition