Canola oil and light cycle oil （LCO） blends were co-hydrotreated over a commercial hydrotreating catalyst （NiMo/Al2O3） to produce diesel fuel with a green diesel component. High hydrodeoxygenation, hydrodesul- phu...Canola oil and light cycle oil （LCO） blends were co-hydrotreated over a commercial hydrotreating catalyst （NiMo/Al2O3） to produce diesel fuel with a green diesel component. High hydrodeoxygenation, hydrodesul- phurization and hydrodenitrogenation catalytic activities were achieved for all three feedstocks tested in the temperature range of 350-380℃ with a hydrogen pressure of 7 MPa and a gas/oil ratio of 800 nL/L. The hydrocrack- ing conversion of the 360℃ ＋ materials in the feedstocks increased by 5% and 15% when 5 and 7.5 wt-% canola oil was added to the LCO, respectively. Compared to the pure LCO, the cetane index of the diesel product formed from hydrotreating the two canola oil-LCO blends increased by 2.5 and 4, respectively. Due to the higher hydrogen requirement to crack and deoxygenate the triglycerides contained in the canola oil, a higher hydrogen consumption was needed to hydrotreat the canola oil-LCO blends.展开更多
Increasing gasoline production in FCC unit can improve the utilization efficiency of petroleum resources and gain economic benefit.This paper discusses the technical principles for increasing FCC gasoline yield from t...Increasing gasoline production in FCC unit can improve the utilization efficiency of petroleum resources and gain economic benefit.This paper discusses the technical principles for increasing FCC gasoline yield from the aspects of feedstock properties,operating conditions,LCO(light cycle oil)recycling,catalyst selection and reactor type,and illustrates the industrial application examples for maximizing gasoline production.The technical measures,such as optimizing the feedstock,properly increasing the catalyst activity and reaction temperature,recycling LCO or hydrotreated LCO,applying high gasoline yield catalyst,and adopting the two-zone riser reactor,are proposed to enhance the gasoline yield.展开更多
文摘Canola oil and light cycle oil （LCO） blends were co-hydrotreated over a commercial hydrotreating catalyst （NiMo/Al2O3） to produce diesel fuel with a green diesel component. High hydrodeoxygenation, hydrodesul- phurization and hydrodenitrogenation catalytic activities were achieved for all three feedstocks tested in the temperature range of 350-380℃ with a hydrogen pressure of 7 MPa and a gas/oil ratio of 800 nL/L. The hydrocrack- ing conversion of the 360℃ ＋ materials in the feedstocks increased by 5% and 15% when 5 and 7.5 wt-% canola oil was added to the LCO, respectively. Compared to the pure LCO, the cetane index of the diesel product formed from hydrotreating the two canola oil-LCO blends increased by 2.5 and 4, respectively. Due to the higher hydrogen requirement to crack and deoxygenate the triglycerides contained in the canola oil, a higher hydrogen consumption was needed to hydrotreat the canola oil-LCO blends.
文摘Increasing gasoline production in FCC unit can improve the utilization efficiency of petroleum resources and gain economic benefit.This paper discusses the technical principles for increasing FCC gasoline yield from the aspects of feedstock properties,operating conditions,LCO(light cycle oil)recycling,catalyst selection and reactor type,and illustrates the industrial application examples for maximizing gasoline production.The technical measures,such as optimizing the feedstock,properly increasing the catalyst activity and reaction temperature,recycling LCO or hydrotreated LCO,applying high gasoline yield catalyst,and adopting the two-zone riser reactor,are proposed to enhance the gasoline yield.
