301. Kinetics study on residue oil slurry-phase hydrocracking with Fe2O3 catalyst.
- Author
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Cui, Qingyan, Zheng, Bin, Wang, Boshi, Yan, Jianteng, Liu, Jiangyong, Li, Tiesen, Shi, Jie, Wang, Tinghai, and Yue, Yuanyuan
- Subjects
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FERRIC oxide , *COKE (Coal product) , *HYDROCRACKING , *ACTIVATION energy , *SUM of squares - Abstract
• A six-lumped kinetic model was proposed for residue oil slurry phase hydrocracking. • VR converted to naphtha and diesel is dominant based on the kinetic rate constants. • The gas product primarily originates from naphtha. • Sensitivity analysis confirms predicted values consistent with experimental values. To gain a profound understanding of the reaction pathway and the controlling step of residue oil slurry-phase hydrocracking over Fe 2 O 3 catalyst, a six-lumped kinetic model was proposed and employed to acquire the kinetic rate constants based on each fraction yield obtained at 400 to 420 °C under initial H 2 pressures of 8 to 10 MPa for 1 to 3 h. The optimal kinetic rate constant for each step of vacuum residue (VR) conversion process was determined via Levenberg-Marquardt algorithm and the sum of squares error (SSE). The results reveal that VR converted into naphtha and diesel is dominant according to their kinetic rate constants, followed by the conversion of vacuum gas oil (VGO) to diesel, diesel to naphtha, and diesel to gas. Furthermore, the sensitivity analysis confirms a strong agreement between the predicted and experimental values. The combination of kinetic rate constants and activation energy illustrates that the gas product primarily originates from naphtha. Additionally, the higher H 2 pressure effectively mitigates coke deposition by restricting the aggregation of polycyclic aromatics, as evidenced by the increase in the reaction activation energy for the conversion of VR to coke and the analysis of the used catalyst. [ABSTRACT FROM AUTHOR]
- Published
- 2024
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