Abstract: Palm oil is a potential a

Abstract: 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 for 120 min. It was
1
found that at 450°C and N2 flow rate of 100ml.min resulted in the highest yield of gasoline fraction of 28.87%,
1
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.
Key words: Catalytic Cracking Metal Impregnation Palm Oil Zeolite HZSM-5

ผลลัพธ์ (อังกฤษ) 2:

Abstract: Palm Oil is a potential alternative source Energy, since it has long Hydrocarbon chains which is quite
similar to the Hydrocarbon Oil Fossil in chains. Thus, Palm Oil Can be Processed Produce biofuel which May to
replace the non-Renewable Fossil Fuels, such as Gasoline, Diesel Oil and Kerosene. 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 Atomic Absorption Spectroscopy (AAS) which produced a synthesized HZSM-5 Si / Al 198. Brunauer Emmet
Teller (BET) surface Area Analysis Showed that of synthesized catalysts was 21.3524 M2.g 1 and the average
Pore Size. of the catalysts was 13 ° A. Process this 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 Micro Bed
Reactor at temperatures between 350 - 500 ° C and between 100 -160 Ml.min Rates N2 flow for 120 min. It was
1
450 ° C and Found at that flow rate of N2 100ml.min resulted in the highest yield of 28.87% of Gasoline fraction,
1
16.70% 20.01% and Kerosene. diesel oil. The synthesized HZSM-5 catalysts Meet the standard of a Catalyst used
in the catalytic cracking of Vegetable Oil to Produce biofuel.
Key Words: Catalytic Cracking Metal impregnation Palm Oil Zeolite HZSM-5.

ผลลัพธ์ (อังกฤษ) 3:

Abstract: 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 gasoline, as, and kerosene 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 for 120 min. It was.1.Found that at 450 ° C and N2 flow rate of 100ml.min resulted in the highest yield of gasoline fraction, of 28.87%1.16.70% 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.Key words: Catalytic Cracking Metal Impregnation Palm Oil Zeolite HZSM-5.