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Numerical simulation and optimization of gas-solid turbulence flow in a precalciner

机译:分解炉内气固湍流的数值模拟与优化

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To optimize the gas-solid flow field of an actual precalciner, numerical simulation was carried out using operational-based boundary conditions. In Euler coordinate system the gas phase is expressed with k-ε model, in Lagrange coordinate system the solid phase is expressed with Discrete Phase Model (DPM), and the random effects of turbulence on the particle dispersion is accounted for with Discrete Random Walk (DRW) model. The predicted gas velocity field shows that the gas flow rises up spirally, which agrees well with what observed on the actual running precalciner. The calculated raw meal concentration distributions are consistent with the actual conditions, showing a good dispersing condition. By changing the initial tertiary air velocity but fixing the initial flue gas velocity-and vice versa-the predicted results were compared. With the fixed initial flue gas velocity, the tertiary air velocity range between 25 m/s and 30 m/s is suggested. With the the fixed initial tertiary air velocity, it is optimum when the flue gas velocity is between 25 m/s and 35 m/s.
机译:为了优化实际分解炉的气固流场,使用基于操作的边界条件进行了数值模拟。在Euler坐标系中,气相用k-ε模型表示,在Lagrange坐标系中,固相用离散相模型(DPM)表示,湍流对颗粒弥散的随机影响由离散随机游走( DRW)模型。预测的气体速度场显示气流呈螺旋形上升,这与在实际运行的分解炉上观察到的相吻合。计算出的粗粉浓度分布与实际情况一致,显示出良好的分散状态。通过更改初始三次风的速度但固定初始烟气的速度(反之亦然),比较了预测结果。在初始烟气速度固定的情况下,建议的三次风速度范围为25 m / s至30 m / s。在固定的初始第三空气速度下,烟道气速度在25 m / s至35 m / s之间时是最佳的。

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