Eight-lumped kinetic model for Fischer-Tropsch wax catalytic cracking and riser reactor simulation

Wax produced during Fischer-Tropsch synthesis (FTS) has no sulfur, nitrogen and aromatic contents and could be an attractive material to produce high quality transportation fuels by means of fluid catalytic cracking reaction. The kinetic modeling and riser reactor simulation are urgently needed. However, most of the current models in this field are based on crude oil feedstock which can not rigorously reflect the features of FTS wax catalytic cracking, especially the aromatization of the cracked light olefins for aromatic gasoline components. The effects of operating conditions on the catalytic cracking performance of FTS wax are investigated in a riser reactor with an industrial beta-zeolite based catalyst. An eight-lumped (including paraffins, olefins, naphthenes and aromatics in gasoline, liquefied petroleum gas, dry gas, FTS wax and coke) kinetic model is developed for product selectivity description and riser reactor simulation in FTS wax catalytic cracking. The theoretical prediction is in good agreement with the experimental data. The modeling work is very helpful in reactor scale-up and operating condition optimization of the process.

Automated summary

The study focuses on investigating the effects of operating conditions on the catalytic cracking performance of FTS wax using an industrial beta-zeolite based catalyst in a riser reactor, and developing an eight-lumped kinetic model for product selectivity description and simulation. The theoretical prediction aligns well with experimental data, providing valuable insights for reactor scale-up and operating condition optimization in the process.