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Effect of Preferential Flexibility Angle on Fluidelastic Instability of a Rotated Triangular Tube Bundle

机译:优先柔性角度对旋转三角管束的流化稳定性的影响

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In the operation of shell-and-tube heat exchangers, tube vibration can be induced by fluid flowing over the tube array. The region of concern in Steam Generators (SG) is the upper most U-bend region, where the flow crosses a large number of tubes which can cause significant hydraulic resistance. This hydraulic resistance forces the flow to change direction. As a result the flow leaves the tube bundle at different angles of attack from ranging 0° to 90°. From a fluidelastic instability point of view, the tube bundle is excited by oblique cross flow. The purpose of this paper is to examine the instability phenomena in a rotated triangle tube bundle subjected to oblique single phase cross flow. Based on experimental mode shapes and measured fluidelastic forces, Connors [1] developed a simple stability criterion for a tube bundle subjected to cross flow: U{sub}c/fD = K(2πζm/ρD{sup}2){sup}b (1) where, fluidelastic instability is expressed in terms of a dimensionless velocity, U{sub}c/fD, and a dimensionless mass-damping term, 2πζm/ρD{sup}2, U{sub}c is the critical pitch velocity for fluidelastic instability, f the tube natural frequency, D the tube diameter, ζ the damping ratio, ρ the density of the fluid, and m the tube mass per unit length, which includes the hydrodynamic mass and the mass of the fluid inside the tube. In the simplest model, the exponent b is 0.5. Generally the exponent depends on tube bundle configuration and dimensionless mass damping term [2]. The fluidelastic instability constant K is usually determined experimentally.
机译:在壳管热交换器的操作中,可以通过流过管阵列的流体诱导管振动。蒸汽发生器(SG)的关注区域是最高U型弯曲区域,其中流过大量的管,这可能导致显着的液压阻力。这种液压阻力迫使流动改变方向。结果,流量使管束以0°至90°的不同攻击角处。从流动的不稳定性的角度来看,管束被倾斜交叉流动激发。本文的目的是检查经受倾斜单相交叉流量的旋转三角管束中的不稳定性现象。基于实验模式的形状和测量的流化力,连接器[1]开发了对经过交叉流量的管束的简单稳定性标准:U {Sub} C / FD = K(2πζm/ρd{sup} 2){sup} b (1)根据无量纲速度,U {Sub} C / FD和无量纲质量阻尼术语,2πμm/ρd{sup} 2表示,流化弹性不稳定性,U {sub} c是临界间距速度用于流化的不稳定性,F管固定频率,D管直径,ζ阻尼比,ρ的液体密度,并且每单位长度的管质量,包括水动力质量和管内的流体的质量。在最简单的模型中,指数B为0.5。通常,指数取决于管束配置和无量纲质量阻尼术语[2]。流动性不稳定性常数K通常在实验上确定。

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