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VORTEX TRAY FOR ADIABATIC AND NONADIABATIC FRACTIONATION

机译:用于绝热和非气体分级的涡流托盘

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摘要

The operating parameters of a tray having new vortex contact devices for adiabatic and nonadiabatic fractionation are investigated. In the vortex device, the vapor moves through tangential channels of the vortex tray for adiabatic and nonadiabatic fractionation, acquires swirling motion, and disperses in the fluids, forming thereby a swirling gas-liquid layer where intense heat and mass transfer takes place. Such a tray design ensures a small fluid volume in the stage and intimate mixing of the gas-liquid mixture. The investigations showed high productivity and efficiency of the vortex tray in a wide gas (vapor) load variation range. The parameters of the swirling gas-liquid layer, such as height, gas content, angular velocity, hydraulic resistance, phase contact area, and coefficient of mass transfer are determined, and an equation is proposed for their calculation. The experimental investigations of the vortex tray efficiency for adiabatic and nonadiabatic fractionation demonstrated that mass transfer in the vapor phase is intensified in nonadiabatic conditions.
机译:研究了具有用于绝热和非等压分馏的新型涡旋接触装置的托盘的操作参数。在涡流装置中,蒸汽通过涡流托盘的切向通道,用于绝热和非气体分级,获取旋转运动,并分散在流体中,从而形成旋转的气液层,其中发生强热和传质。这种托盘设计确保了在阶段中的小流体体积和气液混合物的紧密混合。该研究表明,在宽气体(蒸汽)负载变化范围内的涡流托盘的高生产率和效率。确定旋流气液层的参数,例如高度,气体含量,角速度,液压阻力,相位接触面积和传质系数,并且提出了一种等式的计算。绝热和非等离分馏涡流托盘效率的实验研究表明,在非等压条件下加剧了气相中的传质转移。

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