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GAS-LIQUID SEPARATION DEVICE AND REFRIGERATION DEVICE INCLUDING GAS-LIQUID SEPARATION DEVICE

机译:气液分离装置和制冷装置,包括气液分离装置

摘要

PROBLEM TO BE SOLVED: To solve the problem in which various types of means are adopted regarding improvement in separation performance in a conventional gas-liquid separation device, however, there has been no proposal about how to prevent a gas phase from being mixed with a liquid phase and leaking from a liquid phase outlet pipe, by paying attention to a behavior of a gas phase swirl.SOLUTION: In a gas-liquid separation device, a swirling force is added to a two-phase flow introduced in a cylindrical container from a two-phase flow inlet pipe, a gas and a liquid are separated by a centrifugal force, and a gas phase is flowed out from a gas phase outlet pipe and a liquid phase is flowed out from a liquid phase outlet pipe. A downward conical inclined surface part is formed in which an apex angle is 120 degrees or less in a cross section including a central axis of a cylindrical part, and the liquid outlet pipe is provided at a position of the inclined surface part excluding a connection curved surface provided between the inclined surface part and the cylindrical part of the cylindrical container. Also, in the cross section including the central axis of the cylindrical part, when a ridge line between a cylindrical part inner wall 2b and a connection curved surface inner wall 13a is defined as X, a distance between the ridge line X and the central axis of the cylindrical part is defined as L, and a distance between the ridge line X and a central axis of the liquid phase outlet pipe is defined as L, L/L0.6 is satisfied.SELECTED DRAWING: Figure 5
机译:要解决的问题:为了解决在常规气液分离装置中采用各种类型的装置来提高分离性能的问题,但是,还没有关于如何防止气相与气相混合的提议。液相和从液相出口管泄漏,要注意气相旋涡的行为。解决方案:在气液分离装置中,旋涡力被添加到从圆筒形容器中引入的两相流中在两相流入口管中,气体和液体在离心力的作用下分离,气相从气相出口管流出,液相从液相出口管流出。形成向下的圆锥形倾斜表面部分,其中在包括圆筒形部分的中心轴线的横截面中顶角为120度或更小,并且液体出口管设置在倾斜表面部分的不包括连接弯曲的位置处。设置在圆柱形容器的倾斜表面部分和圆柱形部分之间的表面。另外,在包括圆筒部的中心轴的截面中,将圆筒部内壁2b与连接曲面内壁13a之间的棱线定义为X时,棱线X与中心轴之间的距离将圆筒部的“ L”定义为L,将棱线X与液相出口管的中心轴之间的距离定义为L,满足L / L <0.6。图5

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