Reactor Model for Heavy Oil Hydrotreating with Catalyst Deactivation Based on Vanadium and Coke Deposition

被引:2
|
作者
Jurado, Javier [1 ]
Ancheyta, Jorge [1 ,2 ]
机构
[1] Inst Politecn Nacl, Escuela Super Ingn Quim & Ind Extract, Unidad Profes Adolfo Lopez Mateos, Mexico City 07738, Mexico
[2] Inst Mexicano Petr, Mexico City 07730, Mexico
关键词
HYDROPROCESSING MULTICATALYST DEACTIVATION; SIMULATION; STATE;
D O I
10.1021/acs.energyfuels.2c00876
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
A quasi-dynamic one-dimensional pseudohomogeneous trickle-bed reactor model for hydrotreating of heavy vacuum residue was developed. The model includes catalyst deactivation based on the concentration of impurities in heavy oil as well as coke and vanadium deposition on the catalyst surface during time-on-stream. The concentrations of sulfur and vanadium in products and on the catalyst surface were considered in the objective function based on squared differences between calculated and experimental values to determine the model parameters. Literature experimental data of heavy vacuum residue hydrotreating were used for model validation. The proposed model predicted well the typical "S" shape profiles during time-on-stream due to catalyst deactivation for heavy oil hydrotreating.
引用
收藏
页码:11132 / 11141
页数:10
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