Kim, Tae-Ho Gong, Gyeong-Taek Lee, Byung Gwon Lee, Kwan-Young Jeon, Hee-Young Shin, Chae-Ho Kim, Honggon Jung, Kwang-Deog 2024-01-21T03:04:07Z 2024-01-21T03:04:07Z 2021-09-01 2006-05-17 0926-860X https://pubs.kist.re.kr/handle/201004/135506 The iodine-sulfur (IS) cycle has been focused for hydrogen production by water splitting using a very high temperature nuclear reactor (VHTR) which is a high temperature heat source. The nuclear energy was absorbed at the temperature ranges of 750-900 degrees C by SO3 decomposition reaction to SO2 and O-2 in IS cycle. In this work, the activity of Fe/Al and Fe/Ti catalysts prepared by a co-precipitation was studied in an attempt to find some suitable catalysts for the decomposition of sulfur trioxide as the oxygen-generating reaction in the thermo-chemical water splitting process. The SO3 decomposition was performed in the temperature range of 750-950 degrees C at a space velocity of 72,000 cm(3)/g cat. h in a fixed bed reactor. The catalytic activity of Fe/Al and Fe/Ti catalysts increased with an increase in Fe loadings, indicating that the Fe component should be active. The mechanism for the SO3 decomposition on metal oxides can be described as follows: the metal sulfate formation (MO + SO3 -> MSO4) and the decomposition of metal sulfate (MSO4 -> MO2 + SO2 and MO2 -> MO + 1/2O(2)). (c) 2006 Elsevier B.V. All rights reserved. English ELSEVIER SCIENCE BV HYDROGEN Catalytic decomposition of sulfur trioxide on the binary metal oxide catalysts of Fe/Al and Fe/Ti Article 10.1016/j.apcata.2006.02.052 1 APPLIED CATALYSIS A-GENERAL, v.305, no.1, pp.39 - 45 APPLIED CATALYSIS A-GENERAL 305 1 39 45 scie scopus 000237709300006 2-s2.0-33646487669 Chemistry, Physical Environmental Sciences Chemistry Environmental Sciences & Ecology Article HYDROGEN IS cycle SO3 decomposition metal sulfate decomposition hydrogen production