大自由截面双流板的分析

G. Taranenko
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引用次数: 0

摘要

研究对象为自由截面较大的双型板。这种板的最大问题之一是效率低,这取决于具有大自由截面的双型板的工作方式。这种板上的气液层由液滴和液体膜表示,它们是分散相。在这种情况下,连续相是气体。在自由截面较大的双流板上,供液不足导致双流板的效率下降。在研究过程中,采用了水动力建模的方法。该方法首先在实验装置中对双流板进行了研究,并根据一定的方法将其结果用于工业板的计算。对大自由截面双流板在大范围气液载荷下的流动特性进行了研究。这些板的工作范围已经确定。结果表明,大自由截面双流板的水力阻力与柱装置直径的关系不大。对于安装在直径D = 0.057, 0.4和2 m的柱上的大自由截面双流板,气液层高度对柱截面气速的依赖关系几乎完全一致。结果表明,采用直径D = 0.057 m的塔可以模拟工业直径大自由截面双流板的操作。例如,在水动力建模过程中,对于通常自由截面的双流板,有必要使用较大直径D = 0.15-0.25 m的大自由截面柱的中试装置,与传统自由截面的双流板相比,可以在更高的气液速度下运行。在高灌溉密度的吸收过程中,建议使用具有大自由截面的双流板。
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Analysis of Dual-Flow Plates with a Large Free Section
The object of research is the dual-type plates with a large free section. One of the most problematic areas of such plates is their low efficiency, which depends on the operating mode of the dual-type plates with a large free section. The gas-liquid layer on such plates is represented by drops and films of liquid, which are the dispersed phase. In this case, the continuous phase is gas. Insufficient liquid supply on dual-flow plates with a large free section leads to a decrease in the efficiency of such plates.

During the research, the method of hydrodynamic modeling was used. This method consists in the fact that the dual-flow plates are investigated first in experimental installations, and their results, according to a certain method, are used to calculate industrial plates.

A study of dual-flow plates with a large free section in a wide range of gas and liquid loads has been car-ried out. The range of work of the plates has been determined. It has been established that the hydraulic resis-tance of the dual-flow plates with a large free section depends little on the diameter of the column apparatus. An almost complete coincidence of the dependence of the height of the gas-liquid layer on the gas velocity in the column cross-section is shown for dual-flow plates with a large free section installed in columns with diameters D = 0.057, 0.4 and 2 m. It is revealed that a column with a diameter of D = 0.057 m can be used to simulate the operation of dual-flow plates with a large free section of industrial diameter. For example, for dual-flow plates of the usual free section during hydrodynamic modeling, it is necessary to use pilot plants with columns of larger diameter D = 0.15–0.25 m with a large free cross-section can operate at significantly higher gas and liquid velo-cities compared to the dual-flow plates with a conventional free cross-section.

The use of dual-flow plates with a large free section is recommended in absorption processes at high irriga-tion densities.
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