International Journal of Hydrogen Energy, Vol.37, No.1, 760-764, 2012
Catalytic decomposition of sulfuric acid on composite oxides and Pt/SiC
Thermochemical iodine sulfur (IS) cycle is one of the most promising massive hydrogen production methods with its high efficient and CO2 free credits. The decomposition reaction of sulfuric acid, one of the three reactions of which IS cycle is composed, is kinetically very slow and needs to proceed in the presence of catalyst. In this work, copper chromite (CuCr2O4) and copper ferrite (CuFe2O4) were prepared and employed as the catalysts for sulfuric acid decomposition, their activities were tested at various space velocities and temperatures, and their lifetimes were tested. To overcome the shortcoming of instability in long-time operation of Pt/Al2O3, Pt was loaded on SiC and its activity and lifetime were evaluated and compared with those of CuCr2O4 and CuFe2O4. Results showed that CuCr2O4 has the highest catalytic activity at higher temperature, while Pt/SiC presented the best stability. In addition, the reasons for the deactivation of these catalysts were explored. It was proposed that the deactivation was attributed to formation of sulfate, agglomeration and specific area decreasing. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
Keywords:Nuclear hydrogen production;Iodine sulfur process;Sulfuric acid decomposition;Composite oxides;Catalysts