TY - JOUR
T1 - Nickel-modified sulfated zirconia catalyst
T2 - Synthesis and application for transforming waste cooking oil into biogasoline via a hydrocracking process
AU - Wijaya, Karna
AU - Utami, Maisari
AU - Damayanti, Ameylia Kris
AU - Tahir, Iqmal
AU - Tikoalu, Alfrets Daniel
AU - Rajagopal, Rajinikanth
AU - Thirupathi, Anand
AU - Ali, Daoud
AU - Alarifi, Saud
AU - Chang, Soon Woong
AU - Ravindran, Balasubramani
PY - 2022/8/15
Y1 - 2022/8/15
N2 - The synthesis of a sulfated zirconia catalyst and its modification with Ni metal was carried out and applied in the hydrocracking of waste cooking oil into biogasoline. The SO4/ZrO2 (SZ) catalyst was synthesized via a hydrothermal process using ZrOCl2·8H2O as a precursor, followed by sulfation using (NH4)2SO4 solution. The catalyst was calcined at a temperature of 600 °C. The obtained SZ catalyst was refluxed in aqueous solutions of Ni(NO3)2 with various Ni loadings (1, 2, and 3 wt% Ni), followed by reducing hydrogen gas at 400 °C to yield Ni/SZ catalysts. The impregnation of Ni on SO4/ZrO2 led to an increase in catalyst acidity, as well as their activity and selectivity for the hydrocracking process. Among ZrO2 and the synthesized catalysts, 1% Ni/SZ has the highest acidity level. The hydrocracking process was performed at 450 °C. The 1% Ni/SZ catalyst was able to selectively produce the gasoline fraction, with the conversion reaching 70.28% gasoline from 80.28% for the total liquid products. As a result, the catalyst was shown to be acceptable for industrial-scale applications.
AB - The synthesis of a sulfated zirconia catalyst and its modification with Ni metal was carried out and applied in the hydrocracking of waste cooking oil into biogasoline. The SO4/ZrO2 (SZ) catalyst was synthesized via a hydrothermal process using ZrOCl2·8H2O as a precursor, followed by sulfation using (NH4)2SO4 solution. The catalyst was calcined at a temperature of 600 °C. The obtained SZ catalyst was refluxed in aqueous solutions of Ni(NO3)2 with various Ni loadings (1, 2, and 3 wt% Ni), followed by reducing hydrogen gas at 400 °C to yield Ni/SZ catalysts. The impregnation of Ni on SO4/ZrO2 led to an increase in catalyst acidity, as well as their activity and selectivity for the hydrocracking process. Among ZrO2 and the synthesized catalysts, 1% Ni/SZ has the highest acidity level. The hydrocracking process was performed at 450 °C. The 1% Ni/SZ catalyst was able to selectively produce the gasoline fraction, with the conversion reaching 70.28% gasoline from 80.28% for the total liquid products. As a result, the catalyst was shown to be acceptable for industrial-scale applications.
KW - Catalytic hydrocracking
KW - Ni impregnation effect
KW - Sulfated zirconia
UR - http://www.scopus.com/inward/record.url?scp=85128204838&partnerID=8YFLogxK
U2 - 10.1016/j.fuel.2022.124152
DO - 10.1016/j.fuel.2022.124152
M3 - Article
AN - SCOPUS:85128204838
SN - 0016-2361
VL - 322
JO - FUEL
JF - FUEL
M1 - 124152
ER -