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Numerical Simulation and Application of Gas Flow Distribution of ESP Transformed to Baghouse in Cement Kiln Head

机译:电除尘器改造成水泥窑头布袋除尘器气流分布的数值模拟及应用

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By using Computational Fluid Dynamics (CFD) method,numerical simulation of gas flow distribution of ESP transform to baghouse in cement kiln head of 6000 t/d production. Through numerically simulation,air volume of every filter bag cell and head-on gas flow velocity distribution of filter bag were displayed. By adjusting the configuration parameter of the gas flow distribution device during the numerical simulation, it gives the result that the manner of installing gas flow distribution device, when the windage of the air volume of every filter bag cell is not more than 5% and the press drop of the dust collector with clean filter bag is 300 Pa. The calculated results showed good agreement with the measured results in the field. The simulation results were carried out by transformation. The dust emission concentration of precipitator is 26.6 mg/m3, and the dust running resistance is less than 1000Pa, can achieve the performance assessment requirements.
机译:利用计算流体动力学(CFD)方法,对日产6000吨水泥窑头中ESP转化为布袋除尘器的气流分布进行了数值模拟。通过数值模拟,显示了每个滤袋单元的风量和滤袋正面气流速度分布。通过在数值模拟过程中调整气流分配装置的配置参数,得出的结果是,当每个滤袋单元的风量不大于5%且风量不超过5%时,气流分配装置的安装方式为:带有干净滤袋的集尘器的压降为300 Pa。计算结果与现场实测结果吻合良好。仿真结果通过变换进行。除尘器的粉尘排放浓度为26.6 mg / m3,粉尘运行阻力小于1000Pa,可以达到性能评估要求。

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