崔海蛟, 陈世强, 郑旭, 雒存垚. 上喷式扩散塔喷淋装置热回收与除尘理论模型构建及求解[J]. 煤炭学报, 2021, 46(11): 3590-3598.
引用本文: 崔海蛟, 陈世强, 郑旭, 雒存垚. 上喷式扩散塔喷淋装置热回收与除尘理论模型构建及求解[J]. 煤炭学报, 2021, 46(11): 3590-3598.
CUI Haijiao, CHEN Shiqiang, ZHENG Xu, LUO Cunyao. Establishment and solution of heat recovery and dust removal model of the upperspraying device attached to a mine fan diffuser[J]. Journal of China Coal Society, 2021, 46(11): 3590-3598.
Citation: CUI Haijiao, CHEN Shiqiang, ZHENG Xu, LUO Cunyao. Establishment and solution of heat recovery and dust removal model of the upperspraying device attached to a mine fan diffuser[J]. Journal of China Coal Society, 2021, 46(11): 3590-3598.

上喷式扩散塔喷淋装置热回收与除尘理论模型构建及求解

Establishment and solution of heat recovery and dust removal model of the upperspraying device attached to a mine fan diffuser

  • 摘要: 矿井排风蕴含大量低温热能和粉尘。利用扩散塔喷淋装置,可回收矿井排风热能并捕集排风中的粉尘。针对上喷式扩散塔喷淋装置内排风与上升和下落水滴群传热传质问题及水滴群洗涤含尘排风问题,构建并验证了装置热回收及除尘理论模型。在MATLAB平台上利用四阶五阶Runge-Kutta算法对模型进行求解,获得装置内空气温度、湿度、水滴温度、水滴速度、雷诺数、传热系数、传质系数、粉尘浓度沿扩散塔塔高分布及不同直径尘粒绕单个液滴运动轨迹。研究结果表明,上升水滴传热系数和传质系数在水滴上升过程中先减小后增大,下落水滴的传热系数和传质系数在水滴下落过程中逐渐增大并趋于稳定;上升水滴的温度变化、传热系数及传质系数小于下落水滴,表明上升水滴群对热回收的贡献小于下落水滴群。喷嘴上部区域传热效果优于喷嘴下部区域,为提高装置热回收性能,应延长喷嘴上部换热区域;当气液间相对速度增大时,单个水滴的尘粒捕集效率增大;受气液间相对速度的影响,下落水滴群对除尘的贡献大于上升水滴群;尘粒直径越小,粉尘数浓度在最大液滴上升高度附近的变化速率就越快;除尘效率随着尘粒直径的增大而增大,在风速4 m/s、水滴直径1.7 mm、水滴速度6.5 m/s,水汽质量比0.56的情况下,装置对2.5,5.0和10.0 μm直径尘粒的除尘效率分别为29.2%,73.4%和87.6%。上喷式扩散塔喷淋装置热回收与除尘理论模型的构建和求解为装置性能评估、特性分析、参数设计及运行管理奠定了理论基础。

     

    Abstract: Mine exhaust air contains a large amount of low-temperature heat and dust.Using the spraying device attached to a mine fan diffuser,the heat energy of mine exhaust can be recovered and the dust in the exhaust can be captured.Aiming at the heat and mass transfer problems among air exhaust, rising droplets and falling droplets, as well as the problem of dust removal by droplets in the upper spraying device attached to a mine fan diffuser, a heat recovery model and a dust removal model were constructed and validated.Using the fourth-fifth-order Runge-Kutta algorithm on the MATLAB platform, the constructed models were solved, and the distributions of air temperature, humidity, droplet temperature, droplet velocity, Reynolds number, heat transfer coefficient, mass transfer coefficient and dust concentration along diffuser height were determined.Also, the trajectories of dusts of different diameters around a single droplet were determined.The research results show that the heat transfer coefficient and mass transfer coefficient of rising droplets first decrease and then increase during the droplet ascending process, while the heat transfer coefficient and mass transfer coefficient of falling droplets gradually increase and become stable during the droplet falling process.The temperature change, heat transfer coefficient and mass transfer coefficient of rising droplets are smaller than those of falling droplets, indicating that the contribution of rising droplets to heat recovery is less than that of falling droplets.The heat and mass transfer above nozzles is better than that below nozzles, so to improve thermal performance, the heat transfer area above nozzles should be extended.When the relative velocity between gas and liquid increases, the dust removal efficiency of a single droplet increases.Owing to the influence of the relative velocity between gas and liquid, the contribution of falling droplets to dust removal is greater than that of rising droplets.The smaller the dust diameter, the faster the dust concentration variation rate near the maximum droplet rising height.The dust removal efficiency increases with the increase of dust diameter.The dust removal efficiencies of 2.5, 5.0 and 10.0 μm dusts are 29.2%, 73.4% and 87.6%, respectively (air velocity 4 m/s, droplet diameter 1.7 mm, droplet initial velocity 6.5 m/s, liquid to gas ratio 0.56).The establishment and solution of the model build a theoretical foundation for the performance evaluation, characteristic analysis, parameter design, and operation management of the upper spraying device attached to a mine fan diffuser.

     

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