TY - GEN
T1 - KINETIC ANALYSIS OF C4 ALKANE AND ALKENE PYROLYSIS
T2 - ASME 2008 6th International Conference on Fuel Cell Science, Engineering and Technology, FUELCELL 2008
AU - Al Shoaibi, Ahmed
AU - Dean, Anthony M.
N1 - Funding Information:
This work was partially supported by the DoD Multidisciplinary University Research Initiative (MURI) Program administered by the Office of Naval Research under Grant N00014-02-1-0665. This work was partially supported by AbuDhabi National Oil Company (ADNOC).
Publisher Copyright:
© 2022 by ASME.
PY - 2008
Y1 - 2008
N2 - Pyrolysis experiments of isobutane, isobutylene, and 1-butene were performed over a temperature range of 550-750 oC and a pressure of ~ 0.8 atm. The residence time was ~ 5 s. The fuel conversion and product selectivity were analyzed at these temperatures. The pyrolysis experiments were performed to simulate the gas phase chemistry that occurs in the anode channel of a solid-oxide fuel cell. The experimental results confirm that molecular structure has a substantial impact on pyrolysis kinetics. The experimental data show considerable amounts of C5 and higher species (~2.8 mole % with isobutane at 750 oC, ~7.5 mole % with isobutylene at 737.5 oC, and ~7.4 mole % with 1-butene at 700 oC). The C5+ species are likely deposit precursors. The results confirm that hydrocarbon gas phase kinetics have substantial impact on SOFC operation.
AB - Pyrolysis experiments of isobutane, isobutylene, and 1-butene were performed over a temperature range of 550-750 oC and a pressure of ~ 0.8 atm. The residence time was ~ 5 s. The fuel conversion and product selectivity were analyzed at these temperatures. The pyrolysis experiments were performed to simulate the gas phase chemistry that occurs in the anode channel of a solid-oxide fuel cell. The experimental results confirm that molecular structure has a substantial impact on pyrolysis kinetics. The experimental data show considerable amounts of C5 and higher species (~2.8 mole % with isobutane at 750 oC, ~7.5 mole % with isobutylene at 737.5 oC, and ~7.4 mole % with 1-butene at 700 oC). The C5+ species are likely deposit precursors. The results confirm that hydrocarbon gas phase kinetics have substantial impact on SOFC operation.
UR - http://www.scopus.com/inward/record.url?scp=85148056850&partnerID=8YFLogxK
U2 - 10.1115/FuelCell2008-65033
DO - 10.1115/FuelCell2008-65033
M3 - Conference contribution
AN - SCOPUS:77952646895
T3 - ASME 2008 6th International Conference on Fuel Cell Science, Engineering and Technology, FUELCELL 2008
SP - 143
EP - 153
BT - ASME 2008 6th International Conference on Fuel Cell Science, Engineering and Technology, FUELCELL 2008
Y2 - 16 June 2008 through 18 June 2008
ER -