Тривимірне моделювання сепараційних градієнтних аерозольних технологій. Масловіддільники систем суфлювання ГТД з витратою газу до 800 м3 / ч

Sehriy S. Ryzhkov
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Abstract

There have been implemented separation gradient aerosol technologies which take into account all the forces and effects that influence the deposition of finely dispersed particles. Substantiation is provided for the scientific statement of intensification of the gradient processes of the aerosol media transfer in the boundary layers of multipurpose surfaces during cleaning of the dispersed multiphase flows for the development of technical devices enhancing energy saving and ecological purity of power plants. A sectional design scheme and a three-dimensional model of an oil separator in finite elements were developed for calculating the hydrodynamics and separation. The hydrodynamic situation and the trajectory of the particles in the flow section of the oil separator are calculated. According to the calculation of the velocity distribution in the oil separator at G = 100...200 m3/h, the velocity in the coagulation profile does not exceed 10 m/s. On the basis of the results of the static pressure distribution for G = 100, 200 m3/h, it is established that the pressure difference in the separating coagulators reaches 2.5...3.9 kPa, respectively. The calculation results at G = 100...200 m3/h show that the total pulsation effect of precipitation of the highly dispersed particles makes up 25.1%. Using the calculations, a prototype oil separator was created; its experimental studies were performed on the stand in the form of an open-type wind tunnel. The coefficient of the total purification efficiency is determined, which reaches 99.9%. On the basis of the separation gradient aerosol technologies, it is possible to improve cleaners capturing aerosols in various power plant systems. The performed studies allow further developing a line-up of separators for the gas flow rate from 20 to 2000 m3/h.
已经实施了分离梯度气溶胶技术,该技术考虑了影响精细分散颗粒沉积的所有力和效应。为分散多相流清洗过程中多用途表面边界层气溶胶介质转移梯度过程的强化提供了科学依据,为开发提高电厂节能和生态纯度的技术装置提供了依据。建立了油分离器的截面设计方案和三维有限元模型,用于流体力学和分离计算。计算了油分离器流段内的流体动力情况和颗粒运动轨迹。根据G = 100时油分离器内速度分布的计算200m3 /h,混凝剖面内流速不超过10m /s。根据G = 100、200 m3/h时的静压分布结果,确定了分离絮凝器的压差分别为2.5、3.9 kPa。在G = 100时的计算结果…200 m3/h时,高分散颗粒析出的脉动效应占25.1%。通过计算,制作了一个原型油分离器;其实验研究是在支架上以开式风洞形式进行的。确定了总净化效率系数,达到99.9%。在分离梯度气溶胶技术的基础上,可以改进各种发电厂系统中捕获气溶胶的清洁器。所进行的研究允许进一步开发一系列分离器,以满足20至2000 m3/h的气体流速。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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