Abstract:
Aiming at the low organic sulfur hydrolysis rate in the Claus secondary reactor of sulfur recovery unit, a medium-temperature organic sulfur hydrolysis catalyst was developed adopting the new co-dip technology. The effects of temperature and sulfur resistance performance of the catalyst on the catalyst performance were investigated. The experimental results showed that the catalysts exhibited higher organic sulfur hydrolysisability in the temperature range of 220-300 ℃, which were better than the activated alumina catalyst loaded in the secondary reactor in the change range of H
2S, SO
2 and CS
2 volume fraction.