蓄热式换热器
计算流体力学
过程(计算)
机械工程
工艺工程
材料科学
机械
模拟
核工程
热交换器
工程类
计算机科学
物理
操作系统
作者
Hanbin Zhong,Jing Chen,Fei Gao,Juntao Zhang,Yuqin Zhu,Ben Niu
标识
DOI:10.1515/ijcre-2021-0249
摘要
Abstract The 3D virtual full-loop CFD simulation method with two-fluid model (TFM) was developed to model an industrial two-stage FCC reaction–regeneration system. The virtual connections (mass, species, and energy) between riser reactors, disengager, stripper, and regenerator were realized by defining user-defined functions (UDFs) for boundary conditions according to the reality. Five correction factors were used to correct the reaction rates in the 14-lump FCC reaction kinetics, and two correction factors were used to correct the FCC reaction heat in the first and second riser reactors. As a result, the whole FCC reaction–regeneration system was successfully modeled in one single CFD case. A thorough and comprehensive view of the performance of reaction–regeneration system was obtained by the 3D virtual full-loop CFD simulation, which is helpful for the operating and optimization of FCC unit. The major predicted results were in a good agreement with the industrial data. The effects of operating conditions were also investigated by changing regenerated temperature, catalyst to oil (CTO) ratio, and process capacity.
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