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dc.contributor.authorAhmed Al Shoaibi
dc.contributor.authorAnthony M. Dean
dc.date.accessioned2017-05-09T00:38:29Z
dc.date.available2017-05-09T00:38:29Z
dc.date.copyrightAugust, 2010
dc.date.issued2010
dc.identifier.issn2381-6872
dc.identifier.otherJFCSAU-28943#041015_1.pdf
dc.identifier.urihttp://yetl.yabesh.ir/yetl/handle/yetl/143617
dc.description.abstractPyrolysis experiments of isobutane, isobutylene, and 1-butene were performed over a temperature range of 550–750°C 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 (SOFC). 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°C, ∼7.5 mole % with isobutylene at 737.5°C, and ∼7.4 mole % with 1-butene at 700°C). The C5+ species are likely deposit precursors. The results confirm that hydrocarbon gas-phase kinetics have substantial impact on a SOFC operation.
dc.publisherThe American Society of Mechanical Engineers (ASME)
dc.titleKinetic Analysis of C4 Alkane and Alkene Pyrolysis: Implications for SOFC Operation
dc.typeJournal Paper
dc.journal.volume7
dc.journal.issue4
dc.journal.titleJournal of Fuel Cell Science and Technology
dc.identifier.doi10.1115/1.4000677
dc.journal.fristpage41015
dc.identifier.eissn2381-6910
dc.keywordsFuels
dc.keywordsSolid oxide fuel cells
dc.keywordsTemperature
dc.keywordsPyrolysis
dc.keywordsHydrogen
dc.keywordsMethane
dc.keywordsAnodes AND Molecular weight
dc.treeJournal of Fuel Cell Science and Technology:;2010:;volume( 007 ):;issue: 004
dc.contenttypeFulltext


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