首页> 外文会议>ASME international conference on ocean, offshore and arctic engineering >TWO PHASE ANNULAR FLOW APPROXIMATION USING 1-D FLOW EQUATIONS COUPLED WITH A DRIFT FLUX MODEL FOR CONCURRENT FLOW IN VERTICAL OR NEAR VERTICAL CHANNELS
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TWO PHASE ANNULAR FLOW APPROXIMATION USING 1-D FLOW EQUATIONS COUPLED WITH A DRIFT FLUX MODEL FOR CONCURRENT FLOW IN VERTICAL OR NEAR VERTICAL CHANNELS

机译:垂直或近垂直通道同时流动的一维流动方程与漂移通量模型耦合的两相环流近似

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Annular flow is a flow regime of two-phase gas-liquid flow dominated by high gas flowrate moving through the center of the pipe (gas core). In this paper we have developed and studied an innovative phenomenological model which combines the Zuber & Findlay's Drift Flux Model's weighted mean value approach [1] with the 1-D flow approximation equations. The flow is described in terms of a distribution parameter and an averaged local velocity difference between the phases across the pipe cross-section. The average void fraction is calculated as a function of the ratio of weighted mean gas velocity to the weighted mean liquid velocity (Slip ratio) and the drift flux velocity. The void fraction thus estimated is then applied to the 1-D continuity, momentum and energy equations. The equations are solved simultaneously to obtain the pressure gradient. Lastly, we obtain the liquid film thickness using the triangular hydrodynamic relationship between the liquid flow rate, pressure gradient and the liquid film thickness. The thickness of layer obtained, is then used to verify the original estimate of the void fraction. An iterative procedure is used to match the original estimate to the final value. The results from this study were validated against PipeSIM© software and two field measurements conducted on a wet-gas field in Brazil. As opposed to conventional drift flux models which are based on four simultaneous equations, this model relies on three, thereby significantly reducing the computational resources necessary and is more accurate as we account for variable velocities and void fractions across the pipe cross-section.
机译:环形流是两相气液流的一种流动形式,主要由流经管道(气芯)中心的高气体流量控制。在本文中,我们开发并研究了一种创新的现象学模型,该模型结合了Zuber&Findlay的漂移通量模型的加权平均值方法[1]和一维流动近似方程。根据分布参数和整个管道横截面之间各相之间的平均局部速度差来描述流量。计算平均空隙率是加权平均气体速度与加权平均液体速度之比(滑移率)和漂移通量速度的函数。然后将由此估算的空隙率应用于一维连续性,动量和能量方程。同时求解方程,以获得压力梯度。最后,我们利用液体流速,压力梯度和液膜厚度之间的三角流体力学关系来获得液膜厚度。然后,将获得的层的厚度用于验证空隙率的原始估计。使用迭代过程将原始估计值与最终值进行匹配。这项研究的结果已通过PipeSIM©软件进行了验证,并在巴西的一个湿气田进行了两次田间测量。与基于四个联立方程的常规漂移通量模型相反,该模型依赖三个模型,从而显着减少了所需的计算资源,并且由于我们考虑了整个管道横截面的可变速度和空隙率,因此更加准确。

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