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Pressure Effects on Low-Liquid Loading Oil-Gas Flow in Slightly Upward Inclined Pipes: Flow Pattern,Pressure Gradient and Liquid Holdup

机译:低液体装载油气流量的压力效应略向上倾斜管:流动模式,压力梯度和液体储存

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This paper studies the effects of system pressure in oil-gas low-liquid loading flow in a slightly upward inclined pipe configuration using new experimental data acquired in a high-pressure flow loop.Flow rates are representative of the flow in wet gas transport pipelines.Results for flow pattern observations,pressure gradient,liquid holdup and interfacial roughness measurements are presented and compared to available predictive models.The experiments were carried out at three system pressures(1.48,2.17 and 2.86 MPa)in a 0.155 m ID pipe inclined at 2° with the horizontal.Isopar-L oil and nitrogen gas were the working fluids.Liquid superficial velocities ranged from 0.01 to 0.05 m/s while gas superficial velocities ranged from 1.5 to 16 m/s.Measurements included pressure gradient and liquid holdup.Flow visualization and Wire-Mesh Sensor(WMS)data were used to identify the flow patterns.Interfacial roughness was obtained from the WMS data.Three flow patterns were observed: pseudo-slug,stratified and annular.Pseudo-slug is characterized as an intermittent flow where the liquid does not occupy the whole pipe cross-section as the traditional slug flow does.In the annular flow pattern,the bulk of the liquid was observed to flow at the pipe bottom in a stratified configuration,however,a thin liquid film covered the whole pipe circumference.In both stratified and annular flow patterns,the interface between the gas core and the bottom liquid film presented a flat shape.The superficial gas Froude number,FrSg,was found to be an important dimensionless parameter to scale the pressure effects on the measured parameters.In the pseudo-slug flow pattern,the flow is gravitydominated.Pressure gradient is a function of FrSg and vSL.Liquid holdup is independent of vSL and a function of FrSg.In the stratified and annular flow patterns the flow is friction-dominated.Both pressure gradient and liquid holdup are functions of FrSg and vSL.Interfacial roughness measurements show a small variation in the stratified and annular flow patterns.Model comparison gives mixed results,depending on the specific flow conditions.A relation between the measured interfacial roughness and the interfacial friction factor is proposed,and the results agree with existing measurements.
机译:本文研究了使用在高压流回路中获取的新的实验数据在略微向上倾斜管结构中的油气低液体加载流动对油气低液体加载流动的影响。流速代表潮湿气体输送管道的流量。提出并与可用预测模型进行了流动模式观测,压力梯度,液体储量和界面粗糙度测量的结果。在0.155M ID管中,在2个系统压力(1.48,2.17和2.86MPa)下进行实验°带有水平的。近距离油和氮气是工作流体。浅表速度范围为0.01至0.05米/秒,而气体表观速度范围为1.5至16米/秒。速度包括压力梯度和液体Holdup.flow可视化和线网传感器(WMS)数据用于识别流动模式。从WMS数据获得接口粗糙度。观察到的流动模式:伪粘合剂,str atified和环形.pseudo-slug的特征在于作为传统的块流的液体不占据整个管道横截面的间歇流。在环形流动模式中,观察到液体的大部分流动然而,底部以分层构造,薄型液体膜覆盖了整个管圆形。在分层和环形流动模式中,气体芯和底部液体膜之间的界面呈现平坦的形状。浅表气体FRoude号码,FRSG,被发现是一个重要的无量纲参数,用于缩放对测量参数的压力效应。在伪块流模式下,流量是重力。压力梯度是FRSG和VSL.Liquid Holdup的函数与VSL和函数无关FRSG.IN分层和环形流动模式流动是摩擦统治的。压力梯度和液体储存是FRSG和VSL.Interfacial粗糙度测量的函数展示了一个小varia在分层和环形流动图案中的速度比较,比较给出混合结果,取决于特定的流动条件。提出了测量的界面粗糙度和界面摩擦因子之间的关系,结果与现有的测量结果一致。

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