首页> 外文会议>International Conference on Circulating Fluidized Beds; 20050510-13; Hangzhou(CN) >BOTTOM AND EXIT REGION SOLIDS HOLD-UPS IN CIRCULATING FLUIDIZED BED RISERS
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BOTTOM AND EXIT REGION SOLIDS HOLD-UPS IN CIRCULATING FLUIDIZED BED RISERS

机译:底部和出口区域导致流化床上升的原因

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Data obtained under high density/high solids flux conditions in this work and from the literature are used to develop two new correlations for solids hold-up in the bottom and exit regions of CFB risers. The data cover a wide range of particle sizes and densities and were obtained from risers up to 400 mm in diameter and 15.8 m in height for gas velocities and solids circulation fluxes up to 11 m/s and up to 425 kg/m~2s, respectively. The correlations are incorporated in a one-dimensional model and used to calculate cross-sectional mean solids hold-up profiles along the height of a 76 mm diameter riser used in the study, resulting in good agreement between predicted values and experimental data.
机译:在这项工作中,从高密度/高固含量通量条件下获得的数据以及从文献中获得的数据可用于为CFB立管底部和出口区域中的固体滞留量开发两个新的关联。该数据涵盖了各种粒径和密度,是从直径最大为400 mm,高度为15.8 m的立管获得的,其气体速度和固体循环通量分别为11 m / s和425 kg / m〜2s,分别。相关关系被纳入一维模型中,并用于计算沿研究中使用的直径为76 mm立管的高度的横截面平均固体滞留量,从而在预测值和实验数据之间取得了很好的一致性。

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