2008 Annual Meeting
(328b) Low Temperature Production of SO2 from H2SO4 In the Si Thermochemical Cycle by Using Iron(III) Sulfate Intermediate
Authors
Salvatore Sau, ENEA
Pietro Tarquini, ENEA
Pier Paolo Prosini, ENEA
Alberto Giaconia, ENEA
Giampaolo Caputo, ENEA
Raffaele Liberatore, ENEA
Michela Lanchi, ENEA
Decomposition of sulphuric acid is the highest temperature step in the sulphur iodine water splitting thermochemical cycle. We propose a variation based on the following reactions:
3 H2SO4(acq,conc) + Fe2O3 -> Fe2(SO4)3 (300 °C)
Fe2(SO4)3 -> Fe2O3 + x SO2 + ySO3 + y/2 O2 (650 °C, where x+y=3)
In comparison with direct sulphuric acid decomposition the maximum temperature is lowered, there is no more need for catalysts and the material costs for the reactor is drastically reduced. One disadvantage is the increase of energy demand.
Experimental and theoretical modeling results are presented and discussed.