Show simple item record

dc.contributor.authorWu, Xiao-Yu
dc.contributor.authorChang, Le
dc.contributor.authorUddi, Mruthunjaya
dc.contributor.authorKirchen, Patrick
dc.contributor.authorGhoniem, Ahmed F.
dc.date.accessioned2016-02-28T06:34:58Z
dc.date.available2016-02-28T06:34:58Z
dc.date.issued2015
dc.identifier.citationWu X-Y, Chang L, Uddi M, Kirchen P, Ghoniem AF (2015) Toward enhanced hydrogen generation from water using oxygen permeating LCF membranes. Phys Chem Chem Phys 17: 10093–10107. Available: http://dx.doi.org/10.1039/c5cp00584a.
dc.identifier.issn1463-9076
dc.identifier.issn1463-9084
dc.identifier.pmid25790173
dc.identifier.doi10.1039/c5cp00584a
dc.identifier.urihttp://hdl.handle.net/10754/600045
dc.description.abstract© the Owner Societies. Hydrogen production from water thermolysis can be enhanced by the use of perovskite-type mixed ionic and electronic conducting (MIEC) membranes, through which oxygen permeation is driven by a chemical potential gradient. In this work, water thermolysis experiments were performed using 0.9 mm thick La0.9Ca0.1FeO3-δ (LCF-91) perovskite membranes at 990 °C in a lab-scale button-cell reactor. We examined the effects of the operating conditions such as the gas species concentrations and flow rates on the feed and sweep sides on the water thermolysis rate and oxygen flux. A single step reaction mechanism is proposed for surface reactions, and three-resistance permeation models are derived. Results show that water thermolysis is facilitated by the LCF-91 membrane especially when a fuel is added to the sweep gas. Increasing the gas flow rate and water concentration on the feed side or the hydrogen concentration on the sweep side enhances the hydrogen production rate. In this work, hydrogen is used as the fuel by construction, so that a single-step surface reaction mechanism can be developed and water thermolysis rate parameters can be derived. Both surface reaction rate parameters for oxygen incorporation/dissociation and hydrogen-oxygen reactions are fitted at 990 °C. We compare the oxygen fluxes in water thermolysis and air separation experiments, and identify different limiting steps in the processes involving various oxygen sources and sweep gases for this 0.9 mm thick LCF-91 membrane. In the air feed-inert sweep case, the bulk diffusion and sweep side surface reaction are the two limiting steps. In the water feed-inert sweep case, surface reaction on the feed side dominates the oxygen permeation process. Yet in the water feed-fuel sweep case, surface reactions on both the feed and sweep sides are rate determining when hydrogen concentration in the sweep side is in the range of 1-5 vol%. Furthermore, long term studies show that the surface morphology changes and silica impurities have little impact on the oxygen flux for either water thermolysis or air separation. This journal is
dc.description.sponsorshipThe authors would like to thank both Shell and the King Abdullah University of Science and Technology (KAUST) for funding the research.
dc.publisherRoyal Society of Chemistry (RSC)
dc.titleToward enhanced hydrogen generation from water using oxygen permeating LCF membranes
dc.typeArticle
dc.identifier.journalPhys. Chem. Chem. Phys.
dc.contributor.institutionMassachusetts Institute of Technology, Cambridge, United States
dc.contributor.institutionThe University of British Columbia, Vancouver, Canada


This item appears in the following Collection(s)

Show simple item record