circulating fluidized bed (CFB) roasting has good potential for application in desulfurization of high-sulfur bauxite. The gas-solid distribution and reaction during CFB roasting of high-sulfur bauxite were simulated using the computational particle fluid dynamics (CPFD) method. The effect of primary air flow velocity on particle velocity
particle volume distribution
furnace temperature distribution and pressure distribution were investigated. Under the condition of the same total flow of natural gas
the impact of the number of inlets on the desulfurization efficiency
atmosphere mass fraction distribution and temperature distribution in the furnace was further investigated.
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相关作者
Zhongyuan Li
Xingang Li
Hong Sui
Hong Li
Li Xinyu
Song Yiwen
Teng Shenglong
Zeng Dewang
相关机构
School of Chemical Engineering and Technology, Tianjin University
Collaborative Innovation Center of Chemical Science, Engineering National Engineering Research Centre for Distillation Technology
Key Laboratory of Energy Thermal Conversion and Control of Ministry of Education, School of Energy and Environment, Southeast University
State Key Laboratory of Low-carbon Smart Coal-fired Power Generation and Ultra-clean Emission, China Energy Science and Technology Research Institute Co.,Ltd.
School of Safety Science and Engineering, Xi'an University of Science and Technology