Propylene/propane Permeation Properties of Metal-doped Organosilica Membranes with Controlled Network Sizes and Adsorptive Properties

  • KANEZASHI Masakoto
    Dept. of Chemical Engineering, Graduate School of Engineering, Hiroshima University
  • MIYAUCHI Shuji
    Dept. of Chemical Engineering, Graduate School of Engineering, Hiroshima University
  • HAYAKAWA Shinjiro
    Dept. of Applied Chemistry, Graduate School of Engineering, Hiroshima University
  • NAGASAWA Hiroki
    Dept. of Chemical Engineering, Graduate School of Engineering, Hiroshima University
  • YOSHIOKA Tomohisa
    Dept. of Chemical Engineering, Graduate School of Engineering, Hiroshima University
  • TSURU Toshinori
    Dept. of Chemical Engineering, Graduate School of Engineering, Hiroshima University

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Other Title
  • ネットワークサイズと吸着性を制御した金属ドープオルガノシリカ膜のプロピレン/プロパン透過特性
  • Propylene/propane permeation properties of metal-doped organosilica membranes with controlled network size and adsorption properties

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Abstract

<p>Metal-doped organosilica membranes for C3H6/C3H8 separation were fabricated via a sol-gel method. Al and Ag was selected as a doping material in the fabrication of metal-doped bis (triethoxysilyl) methane (BTESM) membranes, and the effects that doping materials exerted on the organosilica network size and on the C3H6/C3H8 permeation properties were evaluated. Gas permeance ratios such as H2/CH4, H2/C3H6, H2/C3H8, and C3H6/C3H8 were approximately independent of Ag concentration, indicating that network size did not change when doped Ag existed as Ag ions in BTESM networks, as suggested by the X-ray absorption fine structure (XAFS) spectrum. On the other hand, when Al was doped into BTESM, each permeance decreased as Al concentration increased, and the selectivity (H2/N2, H2/CH4) increased largely because of enhanced molecular sieving separation by densified networks. Ag-BTESM membranes showed negative values for activation energy (∼−10 kJ mol−1) for C3H6 permeation, which were a much smaller values than those for BTESM (∼−7 kJ mol−1) and Al-BTESM (∼3 kJ mol−1) membranes. BTESM, Al-, and Ag-BTESM membranes showed values for αmix (binary separation) that were higher than those for αsin (single permeation) at 50 °C. For example, Ag-BTESM (Si/Ag = 9/1) membrane showed higher C3H6/C3H8 selectivity (= 32.5) by binary separation than selectivity (∼19) by single permeation at 50 °C, but the selectivity by binary separation was approximately the same, irrespective of a different pressure ratio (feed pressure/permeate pressure).</p>

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