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Effect of synthesis time on physical properties and catalytic activities of synthesized HZSM-5 on the fast pyrolysis of Jatropha waste
Authors:S Vichaphund  D Aht-Ong  V Sricharoenchaikul  D Atong
Institution:1. Department of Materials Science, Faculty of Science, Chulalongkorn University, Bangkok, 10330, Thailand
2. Center of Excellence on Petrochemical and Materials Technology, Chulalongkorn University, Bangkok, 10330, Thailand
3. Department of Environmental Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand
4. Ceramic Technology Research Unit, National Metal and Materials Technology Center, Pathumthani, 12120, Thailand
Abstract:The catalytic fast pyrolysis of Jatropha waste using synthesized HZSM-5 zeolites was investigated using an analytical pyrolysis-GC/MS (Py-GC/MS) technique. HZSM-5 zeolite was successfully synthesized by hydrothermal method at 160 °C with various synthesis times of 0, 24, and 72 h. From the XRD results, the as-synthesized powder before crystallization (HZSM5-0 h) showed the amorphous phase, while samples with synthesis times of 24 and 72 h (HZSM5-24 h and HZSM5-72 h) showed the high crystalline phase of HZSM-5 with the main peaks at the 2θ of 7.9°, 8.8°, 23.1°, 23.7°, and 23.9°. The particle of HZSM5-72 h appeared in cubic-shaped crystal compared to the HZSM5-24 h. HZSM5-72 h had a higher surface area of 625 m2/g with an average larger pore diameter of 27.97 Å and pore volume of 0.28 cm3/g. The effect of biomass to catalyst ratios of 1:1, 1:5, and 1:10 was investigated at 500 °C. It was found that the aromatic and aliphatic selectivity depended on the synthesis time of HZSM-5 reflected in their surface areas, pore sizes, and catalyst content. The highest aromatic and aliphatic hydrocarbon of almost 95 % was obtained when a large amount of HZSM-5 (synthesized for 72 h) was used which could lead to the high heating values of bio-oils. The HZSM5-72 h also contributed to eliminate the undesirable oxygenated compounds such as acids, aldehydes, and ketones. Nevertheless, there are still a few percentages of N-containing components that may require further denitrogenation prior to utilization of the obtained liquid fuel.
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