Numerical comparison of two modes of gas-solid riser operation: Fluid catalytic cracking vs CFB combustor-Reference-Cited by-同舟云学术

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Numerical comparison of two modes of gas-solid riser operation: Fluid catalytic cracking vs CFB combustor

Published:2017-04 Issue: Volume:31 Page:42-48
ISSN:1674-2001
Container-title:Particuology
language:en
Short-container-title:Particuology

Author:

Mei Yifeng,Zhao Mingzhao,Lu Bona,Chen Sheng,Wang Wei

Funder

National Natural Science Foundation of China

Chinese Academy of Sciences

Ministry of Science and Technology of the People’s Republic of China

Publisher

Elsevier BV

Subject

General Chemical Engineering,General Materials Science

Reference58 articles.

1. The role of meso-scale structures in rapid gas–solid flows;Agrawal;Journal of Fluid Mechanics,2001

2. A novel method for determination of choking velocities;Bai;Powder Technology,1998

3. Fine-grid simulations of gas–solids flow in a circulating fluidized bed;Benyahia;AIChE Journal,2012

4. Numerical analysis of a reacting gas/solid flow in the riser section of an industrial fluid catalytic cracking unit;Benyahia;International Journal of Chemical Reactor Engineering,2003

5. Flow regime diagrams for gas–solid fluidization and upward transport;Bi;International Journal of Multiphase Flow,1995

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1. Steady-state multiscale CFD simulation of a circulating fluidized bed riser;Particuology;2024-10

2. Exploring a unified EMMS drag model for gas-solid fluidization;Chemical Engineering Science;2022-04

3. Numerical exploration of the flow regime transition of a novel catalytic cracking reactor and operation mode analysis;Powder Technology;2022-01

4. Application of Wray–Agarwal Turbulence Model for Numerical Simulation of Gas-Solid Flows in Circulating Fluidized Bed Risers;Journal of Energy Resources Technology;2021-07-20

5. Impact of polydispersity on the flow dynamics in the riser of a circulating fluidized bed;Powder Technology;2021-03

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