• Title of article

    Production of FAME by palm oil transesterification via supercritical methanol technology

  • Author/Authors

    Tan، نويسنده , , Kok Tat and Lee، نويسنده , , Keat Teong and Mohamed، نويسنده , , Abdul Rahman، نويسنده ,

  • Issue Information
    روزنامه با شماره پیاپی سال 2009
  • Pages
    4
  • From page
    1096
  • To page
    1099
  • Abstract
    The present study employed non-catalytic supercritical methanol technology to produce biodiesel from palm oil. The research was carried out in a batch-type tube reactor and heated beyond supercritical temperature and pressure of methanol, which are at 239 °C and 8.1 MPa respectively. The effects of temperature, reaction time and molar ratio of methanol to palm oil on the yield of fatty acid methyl esters (FAME) or biodiesel were investigated. The results obtained showed that non-catalytic supercritical methanol technology only required a mere 20 min reaction time to produce more than 70% yield of FAME. Compared to conventional catalytic methods, which required at least 1 h reaction time to obtain similar yield, supercritical methanol technology has been shown to be superior in terms of time and energy consumption. Apart from the shorter reaction time, it was found that separation and purification of the products were simpler since no catalyst is involved in the process. Hence, formation of side products such as soap in catalytic reactions does not occur in the supercritical methanol method.
  • Keywords
    Elaeis guineensis , biodiesel , Non-catalytic
  • Journal title
    Biomass and Bioenergy
  • Serial Year
    2009
  • Journal title
    Biomass and Bioenergy
  • Record number

    1912723