摘要
基于梯度模式的气相亚格子模型以及颗粒动理学理论,考虑大涡模拟中过滤尺度的影响,对气固相间曳力系数进行修正,建立了气固两相流大涡模拟模型,并对提升管内气固两相流动特性进行了数值模拟,合理地预测出了提升管内气固两相环核流动结构,模拟结果与实测结果相吻合。同时,对提升管内的CO2捕捉过程进行了模拟,得到了气体组分分布以及温度场,可为循环流化床反应器的优化设计提供依据。
Based on the gradient sub-grid scale model and the particle kinetic theory,considering the effect of filtering scale during large eddy simulation,the gas-solid drag coefficient was corrected and the gas-solid two phase flow large eddy simulation model was established.Moreover,the behavior of gas-solid two phase flow was simulated,and the core-annular structure in the riser tube was reasonably predicted.The simulation results were consistent with the experimental results.Furthermore,simulation of the CO2 capture process in the riser tube was conducted,and the gas composition and temperature field were obtained,which can provide references for optimization design of the fluidized bed reactor.
出处
《热力发电》
CAS
北大核心
2013年第12期55-58,68,共5页
Thermal Power Generation
关键词
CFB
提升管
气固两相流
大涡模拟
颗粒动理学
气体组分
温度场
CFB
riser tube
gas-solid two phase flow
large eddy simulation
particle kinetic theory
gas composition
temperature field