Application and Optimization of the Two-stage Riser Catalytic Cracking Technology

You, Xuehui; Li, X.; Liu, Yu-Hao; Li, C.; Zhang, J.; Yang, Chaohe

doi:10.1080/10916460701426148

Cited by 2 publications

(1 citation statement)

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“…In this context, a series of novel FCC processes were developed to maximize target products by inventing special catalysts, such as the catalytic pyrolysis process (CPP) [1] and the maximizing gas and gasoline (MGG) [2]. Besides, there also emerged some new processes through reactor transformation, e.g., maximizing iso-paraffins (MIP) [3], flexible dual-riser fluid catalytic cracking (FDFCC) [4], and two-stage riser fluidized catalytic cracking (TSRFCC) [5]. Compared to catalyst development, the reactor innovation also proves to play a big role in reaction performance improvement for such complex reaction systems.…”

Section: Introductionmentioning

confidence: 99%

Two‐Phase and Three‐Phase Modeling of an Industrial Fluidized Bed for Maximizing Iso‐Paraffins

Han

et al. 2022

Chemie Ingenieur Technik

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The maximizing iso-paraffins (MIP) process is a new fluid catalytic cracking route to produce cleaner gasoline. Its major innovation is the diameter-transformed fluidized bed reactor which can be flexibly regulated to multiple distinct reaction zones. This study aims to accurately reveal complex behaviors in MIP reactor by two-phase modeling and three-phase modeling to extend its application. Both simulations of an industrial MIP reactor are compared in terms of solids and liquid concentration, temperature, coke content, gas velocity, and product yield. It is found the two-phase case is enough for predicting the region far away from the oil feedstock injection, and the other is the better choice especially in the first zone if the heat transfer model can be reasonably built.

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