返回
Gas-solid flow characteristics in downstream reactor
DOI:10.1016/j.powtec.2025.121307.png)
摘要
En 中文
• 提出了一种在下游反应器床层中实现“溢流”的判据。
• 阐明了在反应室中实施整体运动的原因。
• 揭示了在整体流动路径不同位置处的床层结构。
• 探讨了不同操作因素对反应室中气固流动特性的影响。
期刊
IF:
4.6
论文数:
2.9K
被引数:
5.3W
机构
暂无机构信息
引用论文
Comprehensive study on cluster characteristics with different particle properties in the diameter-varying fluidized bed reactor对不同粒子特性在直径变化流化床反应器中团聚物特性的综合研究
POWDER TECHNOLOGY
IF4.6
Effect of Gaussian size distribution width on minimum fluidization velocity in tapered gas-solid fluidized beds
PARTICUOLOGY
IF4.3
Fluidization of biomass and inert particle mixtures in a pseudo 2D pressured fluidized bed生物质和惰性颗粒混合物在拟二维加压流化床中的流态化
POWDER TECHNOLOGY
IF4.6
Analysis of gas-solid flow in a pilot-scale main furnace for suspension magnetization roaster悬浮磁化焙烧试验规模主炉内气固流态分析
POWDER TECHNOLOGY
IF4.6
Study on the gas-solid flow and reaction characteristics of oxy-fuel co-firing of coal and biomass in a pressurized fluidized bed by 3D Eulerian-Lagrangian modelling在加压流化床中通过三维欧拉-拉格朗日模型对煤与生物质氧燃料共燃的气固流动和反应特性进行研究
POWDER TECHNOLOGY
IF4.6

