1) stationary bed
静床
2) Static bed height
静床高度
1.
A simple hydrodynamic model,including additional terms in both the gas-and solid-phase momentum equations based on the two-fluid theory by considering particle-fluid interactions under a quasi-equilibrium state,was used to investigate numerically the effects of jet gas velocity,slit size,annular gas velocity and static bed height on the jet penetration depth in gas-solid fluidized beds.
30 m)内射流气速、喷嘴尺寸、环隙气速和静床高度对射流穿透深度的影响,并以树脂颗粒(粒径670μm、密度1474 kg。
3) initial bed height
静床高
1.
5 m/s and different initial bed height ran.
5‰)和环形(α=5‰)气体分布器,以直径154～180μm、密度2550kg/m3的砂子为颗粒,在静床高H0=0。
2.
6 m?s?1, the initial bed heights of 0.
5%的枝条形气体分布器,以直径为154×10-6～180×10-6m、密度为2550kg·m-3的砂子为固体颗粒,压缩空气为流化气体,在静床高为0。
4) still bar
静止针床
5) electrostatic fluidized bed
静电浮床
补充资料：沸腾床燃烧(见流化床燃烧)
沸腾床燃烧(见流化床燃烧)
boiling-bed combustion:see fluidized-bed combustion
沸腾床燃烧(boiling一bed eombustion)见流化床燃烧。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条