• Title of article

    Selective permeation and separation of steam from water–methanol–hydrogen gas mixtures through mordenite membrane

  • Author/Authors

    Ken-Ichi Sawamura، نويسنده , , Tsutomu Shirai، نويسنده , , Mitsuko Takada، نويسنده , , Yasushi Sekine، نويسنده , , Eiichi Kikuchi، نويسنده , , Masahiko Matsukata، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2008
  • Pages
    6
  • From page
    182
  • To page
    187
  • Abstract
    Separation properties of a mordenite membrane for water–methanol–hydrogen mixtures were studied in the temperature range from 423 to 523 K under pressurized conditions. The mordenite membrane was prepared on the outer surface of a porous alumina tubular support by a secondary-growth method. It was found that water was selectively permeated through the membrane. The separation factor of water/hydrogen and water/methanol were 49–156 and 73–101, respectively. Even when only hydrogen was fed at 0.5 MPa, its permeance was as low as 10−9 mol m−2 s−1 Pa−1 up to 493 K, possibly suggesting that water pre-adsorbed in the micropores of mordenite hindered the permeation of hydrogen. The hydrogen permeance dramatically increased to 6.5 × 10−7 mol m−2 s−1 Pa−1 at 503 K and reached to 1.4 × 10−6 mol m−2 s−1 Pa−1 at 523 K because of the formation of cracks in the membrane. However, the membrane was thermally stabilized in the presence of steam and/or methanol.
  • Keywords
    Zeolite membrane , mordenite , membrane reactor , Methanol synthesis , Gas separation
  • Journal title
    CATALYSIS TODAY
  • Serial Year
    2008
  • Journal title
    CATALYSIS TODAY
  • Record number

    1236372