The conversion of palm oil to hydrocarbons using a shape selective zeolite
catalyst is reported in this work. Palm oil was passed over HZSM-5 catalyst
in a fixed bed micro-reactor and the reactor was operated a:. atmospheric
pressure, a temperature range of 360 to 420 degrees C and weight hourly spa
ce velocity (WHSV) of 2 to 4 h(-1). Tie main objective was to study the eff
ect of reaction temperature and oil space velocity on the conversion and se
lectivity of gasoline range hydrocarbons. The results show that 40 to 70wt%
Of the palm oil can be converted to aromatics and hydrocarbons in the gaso
line, diesel and kerosene range, light gases, coke and water. The maximum g
asoline range hydrocarbons yield of 40wt% of total product formed was obtai
ned at 400 degrees C and 2 h(-1) space velocity.