• Login
    View Item 
    •   Home
    • Office of Sponsored Research (OSR)
    • KAUST Funded Research
    • Publications Acknowledging KAUST Support
    • View Item
    •   Home
    • Office of Sponsored Research (OSR)
    • KAUST Funded Research
    • Publications Acknowledging KAUST Support
    • View Item
    JavaScript is disabled for your browser. Some features of this site may not work without it.

    Browse

    All of KAUSTCommunitiesIssue DateSubmit DateThis CollectionIssue DateSubmit Date

    My Account

    Login

    Quick Links

    Open Access PolicyORCID LibguideTheses and Dissertations LibguideSubmit an Item

    Statistics

    Display statistics

    Surface oxygen vacancy and oxygen permeation flux limits of perovskite ion transport membranes

    • CSV
    • RefMan
    • EndNote
    • BibTex
    • RefWorks
    Type
    Article
    Authors
    Hunt, Anton cc
    Dimitrakopoulos, Georgios cc
    Ghoniem, Ahmed F.
    KAUST Grant Number
    KUS-L1-010-01
    Date
    2015-09
    Permanent link to this record
    http://hdl.handle.net/10754/599815
    
    Metadata
    Show full item record
    Abstract
    © 2015 Elsevier B.V. The mechanisms and quantitative models for how oxygen is separated from air using ion transport membranes (ITMs) are not well understood, largely due to the experimental complexity for determining surface exchange reactions at extreme temperatures (>800°C). This is especially true when fuels are present at the permeate surface. For both inert and reactive (fuels) operations, solid-state oxygen surface vacancies (δ) are ultimately responsible for driving the oxygen flux, JO2. In the inert case, the value of δ at either surface is a function of the local PO2 and temperature, whilst the magnitude of δ dictates both the JO2 and the inherent stability of the material. In this study values of δ are presented based on experimental measurements under inert (CO2) sweep: using a permeation flux model and local PO2 measurements, collected by means of a local gas-sampling probe in our large-scale reactor, we can determine δ directly. The ITM assessed was La0.9Ca0.1FeO3-δ (LCF); the relative resistances to JO2 were quantified using the pre-defined permeation flux model and local PO2 values. Across a temperature range from 825°C to 1056°C, δ was found to vary from 0.007 to 0.029 (<1%), safely within material stability limits, whilst the permeate surface exchange resistance dominates. An inert JO2 limit was identified owing to a maximum sweep surface δ, δmaxinert. The physical presence of δmaxinert is attributed to a rate limiting step shift from desorption to associative electron transfer steps on the sweep surface as PO2 is reduced. Permeate surface exchange limitations under non-reactive conditions suggest that reactive (fuel) operation is necessary to accelerate surface chemistry for future work, to reduce flux resistance and push δpast δmaxinert in a stable manner.
    Citation
    Hunt A, Dimitrakopoulos G, Ghoniem AF (2015) Surface oxygen vacancy and oxygen permeation flux limits of perovskite ion transport membranes. Journal of Membrane Science 489: 248–257. Available: http://dx.doi.org/10.1016/j.memsci.2015.03.095.
    Sponsors
    The authors would like to thank the King Fahd University of Petroleum and Minerals (KFUPM) in Dhahran, Saudi Arabia, for partially funding the research reported in this paper through the Center of Clean Water and Clean Energy at the Massachusetts Institute of Technology and KFUPM under project number R2-CE-08. This work is also supported through funding from the King Abdullah University of Science and Technology (KAUST) in Thuwal, Saudi Arabia under project number KUS-L1-010-01. A special thanks is also extended to Air Products and Chemicals, Inc. (APCI) for their guidance in this field and for the sharing of knowledge regarding LCF membranes; additionally the cooperative efforts with Ceramatec to produce the LCF membranes for the experimental reactor in this work are gratefully acknowledged.
    Publisher
    Elsevier BV
    Journal
    Journal of Membrane Science
    DOI
    10.1016/j.memsci.2015.03.095
    ae974a485f413a2113503eed53cd6c53
    10.1016/j.memsci.2015.03.095
    Scopus Count
    Collections
    Publications Acknowledging KAUST Support

    entitlement

     

    Related items

    Showing items related by title, author, creator and subject.

    • Thumbnail

      Oxygen defect-rich double-layer hierarchical porous Co3O4 arrays as high-efficient oxygen evolution catalyst for overall water splitting

      Yan, Puxuan; Huang, Meilin; Wang, Benzhi; Wan, Zixia; Qian, Mancai; Yan, Hu; Isimjan, Tayirjan T.; Tian, Jianniao; Yang, Xiulin (Journal of Energy Chemistry, Elsevier BV, 2020-02-24) [Article]
      Construction of oxygen evolution electrocatalysts with abundant oxygen defects and large specific surface areas can significantly improve the conversion efficiency of overall water splitting. Herein, we adopt a controlled method to prepare oxygen defect-rich double-layer hierarchical porous Co3O4 arrays on nickel foam (DL-Co3O4/NF) for water splitting. The unique array-like structure, crystallinity, porosity, and chemical states have been carefully investigated through SEM, TEM, XRD, BET, and XPS techniques. The designated DL-Co3O4/NF has oxygen defects of up to 67.7% and a large BET surface area (57.4 m2 g−1). Electrochemical studies show that the catalyst only requires an overpotential of 256 mV to reach 20 mA cm−2, as well as a small Tafel slope of 60.8 mV dec−1, which is far better than all control catalysts. Besides, the catalyst also demonstrates excellent overall water splitting performance in a two-electrode system and good long-term stability, far superior to most previously reported catalysts. Electrocatalytic mechanisms indicate that abundant oxygen vacancies provide more active sites and good conductivity. At the same time, the unique porous arrays facilitate electrolyte transport and gas emissions, thereby synergistically improving OER catalytic performance.
    • Thumbnail

      CaMn0.875Ti0.125O3 as oxygen carrier for chemical-looping combustion with oxygen uncoupling (CLOU)—Experiments in a continuously operating fluidized-bed reactor system

      Rydén, Magnus; Lyngfelt, Anders; Mattisson, Tobias (International Journal of Greenhouse Gas Control, Elsevier BV, 2011-03) [Article]
      Particles of the perovskite material CaMn0.875Ti0.125O3 has been examined as oxygen carrier for chemical-looping with oxygen uncoupling, and for chemical-looping combustion of natural gas, by 70h of experiments in a circulating fluidized-bed reactor system. For the oxygen uncoupling experiments, it was found that the particles released O2 in gas phase at temperatures above 720°C when the fuel reactor was fluidized with CO2. The effect increased with increased temperature, and with the O2 partial pressure in the air reactor. At 950°C, the O2 concentration in the outlet from the fuel reactor was in the order of 4.0vol%, if the particles were oxidized in air. For the chemical-looping combustion experiments the combustion efficiency with standard process parameters was in the order of 95% at 950°C, using 1000kg oxygen carrier per MW natural gas, of which about 30% was located in the fuel reactor. Reducing the fuel flow so that 1900kg oxygen carrier per MW natural gas was used improved the combustion efficiency to roughly 99.8%. The particles retained their physical properties, reactivity with CH4 and ability to release gas-phase O2 reasonably well throughout the testing period and there were no problems with the fluidization or formation of solid carbon in the reactor. X-ray diffraction showed that the particles underwent changes in their phase composition though. © 2010 Elsevier Ltd.
    • Thumbnail

      Oxygen-Reducing Biocathodes Operating with Passive Oxygen Transfer in Microbial Fuel Cells

      Xia, Xue; Tokash, Justin C.; Zhang, Fang; Liang, Peng; Huang, Xia; Logan, Bruce E. (Environmental Science & Technology, American Chemical Society (ACS), 2013-02-08) [Article]
      Oxygen-reducing biocathodes previously developed for microbial fuel cells (MFCs) have required energy-intensive aeration of the catholyte. To avoid the need for aeration, the ability of biocathodes to function with passive oxygen transfer was examined here using air cathode MFCs. Two-chamber, air cathode MFCs with biocathodes produced a maximum power density of 554 ± 0 mW/m 2, which was comparable to that obtained with a Pt cathode (576 ± 16 mW/m2), and 38 times higher than that produced without a catalyst (14 ± 3 mW/m2). The maximum current density with biocathodes in this air-cathode MFC was 1.0 A/m2, compared to 0.49 A/m2 originally produced in a two-chamber MFC with an aqueous cathode (with cathode chamber aeration). Single-chamber, air-cathode MFCs with the same biocathodes initially produced higher voltages than those with Pt cathodes, but after several cycles the catalytic activity of the biocathodes was lost. This change in cathode performance resulted from direct exposure of the cathodes to solutions containing high concentrations of organic matter in the single-chamber configuration. Biocathode performance was not impaired in two-chamber designs where the cathode was kept separated from the anode solution. These results demonstrate that direct-air biocathodes can work very well, but only under conditions that minimize heterotrophic growth of microorganisms on the cathodes. © 2013 American Chemical Society.
    DSpace software copyright © 2002-2023  DuraSpace
    Quick Guide | Contact Us | KAUST University Library
    Open Repository is a service hosted by 
    Atmire NV
     

    Export search results

    The export option will allow you to export the current search results of the entered query to a file. Different formats are available for download. To export the items, click on the button corresponding with the preferred download format.

    By default, clicking on the export buttons will result in a download of the allowed maximum amount of items. For anonymous users the allowed maximum amount is 50 search results.

    To select a subset of the search results, click "Selective Export" button and make a selection of the items you want to export. The amount of items that can be exported at once is similarly restricted as the full export.

    After making a selection, click one of the export format buttons. The amount of items that will be exported is indicated in the bubble next to export format.