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Numerical comparison of two modes of gas-solid riser operation: Fluid catalytic cracking vs CFB combustor 被引量:5
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作者 Yifeng Mei Mingzhao Zhao +2 位作者 Bona Lu Sheng Chen Wei Wang 《Particuology》 SCIE EI CAS CSCD 2017年第2期42-48,共7页
Two modes of gas-solid riser operation, i.e., fluid catalytic cracking (FCC) and circulating fluidized bed combustor (CFBC), have been recognized in literature; particularly in the understanding of choking phenome... Two modes of gas-solid riser operation, i.e., fluid catalytic cracking (FCC) and circulating fluidized bed combustor (CFBC), have been recognized in literature; particularly in the understanding of choking phenomena. This work compares these two modes of operation through computational fluid dynamics (CFD) simulation. In CFD simulations, the different operations are represented by fixing appropriate boundary conditions: solids flux or solids inventory. It is found that the FCC and CFBC modes generally have the same dependence of solids flux on the mean solids volume fraction or solids inventory. However, during the choking transition, the FCC mode of operation needs more time to reach a steady state; thus the FCC system may have insufficient time to respond to valve adjustments or flow state change, leading to the choking. The difference between FCC and CFBC systems is more pronounced for the systems with longer risers. A more detailed investigation of these two modes of riser operation may require a three-dimensional full loop simulation with dynamic valve adjustment. 展开更多
关键词 Fluidization Computational fluid dynamics Simulation Fluid catalytic cracking Circulating fluidized bed Choking
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