TY - GEN
T1 - Catalytic decomposition of sulfuric acid for thermochemical water splitting processes
AU - Ginosar, Daniel M.
AU - Anderson, Raymond P.
AU - Glenn, Anne W.
PY - 2004
Y1 - 2004
N2 - The Idaho National Engineering and Environmental Laboratory (INEEL) is currently exploring the limitations of the sulfuric acid decomposition catalyst for the purpose of developing highly active, stable catalysts for a high-temperature catalytic sulfuric acid decomposition reaction step. An overview of the INEEL nuclear hydrogen project was presented, focusing on the sulfuric acid catalytic decomposition studies. To examine catalyst activity and stability, a high-temperature sulfuric acid decomposition reaction system was constructed. The system consists of a sulfuric acid pumping section, a high-temperature SO3 generation zone, a high-temperature catalytic reaction zone, and a product collection section. Results were presented for three catalysts, i.e., Pt/Al2O3, Pt/TiO2, and Pt/ZrO2, with Pt loadings ranging from 0.1 to 1 wt %. Preliminary results exploring the Pt/Al2O3 catalyst between 800° and 850°C showed that sulfuric acid conversions approaching 65% could be achieved; however, the catalyst was not stable and lost a significant level of activity over a 6 hr period. This is an abstract of a paper presented at the 3rd Topical Conference on Fuel Cell Technology at the 2004 AIChE National Spring Meeting (New Orleans, LA, 4/25-29/2004).
AB - The Idaho National Engineering and Environmental Laboratory (INEEL) is currently exploring the limitations of the sulfuric acid decomposition catalyst for the purpose of developing highly active, stable catalysts for a high-temperature catalytic sulfuric acid decomposition reaction step. An overview of the INEEL nuclear hydrogen project was presented, focusing on the sulfuric acid catalytic decomposition studies. To examine catalyst activity and stability, a high-temperature sulfuric acid decomposition reaction system was constructed. The system consists of a sulfuric acid pumping section, a high-temperature SO3 generation zone, a high-temperature catalytic reaction zone, and a product collection section. Results were presented for three catalysts, i.e., Pt/Al2O3, Pt/TiO2, and Pt/ZrO2, with Pt loadings ranging from 0.1 to 1 wt %. Preliminary results exploring the Pt/Al2O3 catalyst between 800° and 850°C showed that sulfuric acid conversions approaching 65% could be achieved; however, the catalyst was not stable and lost a significant level of activity over a 6 hr period. This is an abstract of a paper presented at the 3rd Topical Conference on Fuel Cell Technology at the 2004 AIChE National Spring Meeting (New Orleans, LA, 4/25-29/2004).
KW - Hydrogen Production
KW - Thermochemical
KW - Water-Splitting
UR - https://www.scopus.com/pages/publications/4043087578
M3 - Conference contribution
AN - SCOPUS:4043087578
SN - 0816909423
T3 - 2004 AIChE Spring Meeting, Conference Proceedings
BT - 2004 AIChE Spring Meeting, Conference Proceedings
T2 - 2004 AIChE Spring Meeting, Conference Proceedings
Y2 - 25 April 2004 through 29 April 2004
ER -