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:使用具有1-D流量方程的两个相环形流程近似,耦合与漂移通量模型,用于在垂直或近垂直通道中的并发流动

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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:环形流是由高气体流动穿过管道(气体芯)的高气体流量的两相气体流动的流动状态。在本文中,我们已经开发并研究了一种创新的现象学模型,将Zuber&Findlay的漂移助熔剂模型的加权平均值方法[1]与1-D流近似方程组合在一起。根据分布参数和管道横截面之间的相位之间的平均局部速度差来描述流程。作为加权平均液体速度(滑移比率的重量平均气体速度(滑移比率)和漂移通量速度的函数计算平均空隙部分。然后将如此估计的空隙部分施加到1-D连续性,动量和能量方程。等式同时解决以获得压力梯度。最后,我们使用液体流速,压力梯度和液体膜厚度之间的三角流体动力学关系获得液体膜厚度。然后使用所获得的层的厚度来验证空隙率的原始估计。迭代过程用于将原始估计与最终值匹配。该研究的结果针对Pipesim软件验证,并在巴西的湿法场上进行了两个现场测量。与基于四个同时等式的传统漂移磁通模型相反,该模型依赖于三,从而显着降低所需的计算资源,并且在管道横截面上的可变速度和空隙分数的考虑更准确。

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