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Numerical simulation and experimental studies of external flow field in FCC feed nozzle

机译:FCC进料喷嘴外流场的数值模拟与实验研究

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The present paper focus on spray characteristics and droplet distribution by using the discrete phase model of CFD method for external flow field simulation of fluid catalytic cracking feed nozzle. A two-fluid Euler-Lagrange approach is selected for modeling the aforementioned phenomenon referring to influence of the gas-liquid two phase pressure on atomizing performance, then the two-phase flow taking place inside the mixing chamber and the exterior region near the outlet of the nozzle has been simulated. The results attained by numerical simulation shows that the atomizing particle size decreased with the increase of axial distance, and it obviously decreased near the outlet of nozzle, and then leveled off. In view of the initial structure of catalytic cracking feed atomizing nozzle, the experiment setup was established, experimental results showed that the average atomizing diameter increased with the increase of liquid flow rate and it decreased with the increase of gas supply pressure, the atomizing particle size tend to level off while the gas phase pressure increases to a certain value. Under the operating parameters of that gas phase pressure is 1 bar (0.1MPa) and water flow rate is 16.7g/s, both the numerical simulation and experimental data with a good agreement. The study was of certain referring value on the structure design and operating parameters optimization of catalytic cracking feed nozzle.
机译:本文将离散特征模型用于流体催化裂化进料喷嘴的外部流场模拟,重点研究了CFD方法的离散相模型。选择两流体Euler-Lagrange方法来模拟上述现象,方法是参考气液两相压力对雾化性能的影响,然后两相流发生在混合室内以及靠近出口的外部区域。喷嘴已被模拟。数值模拟结果表明,雾化粒径随轴向距离的增加而减小,在喷嘴出口附近明显减小,然后趋于平稳。针对催化裂化进料雾化喷嘴的初始结构,建立了实验装置,实验结果表明,平均雾化直径随液体流量的增加而增加,随供气压力,雾化粒径的增加而减小。在气相压力增加到一定值时趋于平稳。在气相压力为1 bar(0.1MPa),水流量为16.7g / s的运行参数下,数值模拟和实验数据均吻合良好。该研究对催化裂化进料喷嘴的结构设计和运行参数的优化具有一定的参考价值。

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