TY - JOUR
T1 - Biofuel production from catalytic cracking of palm oil
AU - Sirajudin, Nurjannah
AU - Jusoff, Kamaruzaman
AU - Yani, Setyawati
AU - Ifa, La
AU - Roesyadi, Ahmad
PY - 2013
Y1 - 2013
N2 - Palm oil is a potential alternative energy source, since it has long hydrocarbon chains which is quite similar to the hydrocarbon chains in fossil oil. Thus, palm oil can be processed to produce biofuel which may replace the non-renewable fossil fuels, such as gasoline, kerosene and diesel oil. During utilization, biofuel produces fewer pollutants than fossil fuel. Therefore, biofuel is safer and environmentally friendly. The research was conducted through a catalyst synthesis and the catalytic cracking process. HZSM-5 was synthesized using an Absorption Atomic Spectroscopy (AAS) which produced a synthesized HZSM-5 Si/Al 198. Brunauer Emmet Teller (BET) analysis showed that surface area of synthesized catalysts was 21.3524 m2.g-1 and the average pore size of the catalysts was 13 °A. This process confirmed that the synthesized catalysts meet the requirement as a catalyst used in the catalytic cracking process. The catalytic cracking was carried out in a fixed bed micro reactor at temperatures between 350 - 500 °C and N2 flow rates between 100-160 ml.min-1 for 120 min. It was found that at 450°C and N2 flow rate of 100ml.min-1resulted in the highest yield of gasoline fraction of 28.87%, 16.70% kerosene and 1.20%. diesel oil. The synthesized HZSM-5 catalysts meet the standard of a catalyst used in the catalytic cracking of vegetable oil to produce biofuel.
AB - Palm oil is a potential alternative energy source, since it has long hydrocarbon chains which is quite similar to the hydrocarbon chains in fossil oil. Thus, palm oil can be processed to produce biofuel which may replace the non-renewable fossil fuels, such as gasoline, kerosene and diesel oil. During utilization, biofuel produces fewer pollutants than fossil fuel. Therefore, biofuel is safer and environmentally friendly. The research was conducted through a catalyst synthesis and the catalytic cracking process. HZSM-5 was synthesized using an Absorption Atomic Spectroscopy (AAS) which produced a synthesized HZSM-5 Si/Al 198. Brunauer Emmet Teller (BET) analysis showed that surface area of synthesized catalysts was 21.3524 m2.g-1 and the average pore size of the catalysts was 13 °A. This process confirmed that the synthesized catalysts meet the requirement as a catalyst used in the catalytic cracking process. The catalytic cracking was carried out in a fixed bed micro reactor at temperatures between 350 - 500 °C and N2 flow rates between 100-160 ml.min-1 for 120 min. It was found that at 450°C and N2 flow rate of 100ml.min-1resulted in the highest yield of gasoline fraction of 28.87%, 16.70% kerosene and 1.20%. diesel oil. The synthesized HZSM-5 catalysts meet the standard of a catalyst used in the catalytic cracking of vegetable oil to produce biofuel.
KW - Catalytic cracking
KW - Metal impregnation
KW - Palm oil
KW - Zeolite HZSM-5
UR - http://www.scopus.com/inward/record.url?scp=84891286066&partnerID=8YFLogxK
U2 - 10.5829/idosi.wasj.2013.26.nrrdsi.26012
DO - 10.5829/idosi.wasj.2013.26.nrrdsi.26012
M3 - Article
AN - SCOPUS:84891286066
SN - 1818-4952
VL - 26
SP - 67
EP - 71
JO - World Applied Sciences Journal
JF - World Applied Sciences Journal
IS - 26
ER -