The time-dependent liquid film thickness and pressure drop were measured by using parallel-wire conductance probes and capacitance differential-pressure transducers. Applying the eddy viscosity theory and an appropria...The time-dependent liquid film thickness and pressure drop were measured by using parallel-wire conductance probes and capacitance differential-pressure transducers. Applying the eddy viscosity theory and an appropriate correlation of interfacial sear stress,a new two-dimensional separated model of holdup and pressure drop of turbulent/turbulent gas-liquid stratified flow was presented. Prediction results agreed well with experimental data.展开更多
This paper aims to propose correlations to predict pressure gradient,friction factor and fluid phase hold-up in liquid-liquid horizontal pipe flow.To develop the correlations,experiments are conducted using high visco...This paper aims to propose correlations to predict pressure gradient,friction factor and fluid phase hold-up in liquid-liquid horizontal pipe flow.To develop the correlations,experiments are conducted using high viscous oils(202 and 630 mPa⋅s)in a steel pipe of length 11.25 m and length-to-diameter ratio of 708.In addition,the experimental data from the literature comprising wide range of flow and fluid properties is analyzed.For the analysis,the liquid-liquid pipe flow data is categorized into two as:stratified and dispersed.The existing friction factor correlations are modified to incorporate the effects of viscosity of the oil phase,interfacial curvature(contact/wetting angle-in lieu of material of the pipe)and fluid phase fraction.In the two-fluid model of stratified flow,the wall stress and interfacial stress correlations are substituted with superficial velocities of fluids and superficial Reynolds numbers of fluid phases replacing fluid phase velocities and fluid Reynolds numbers.Similarly,for dispersed flow,an effective Reynolds number is described as the sum of superficial Reynolds number of oil and water phases.Substituting the generally employed mean or mixture Reynolds number with the effective Reynolds number into the existing single-phase turbulent flow friction factor correlation,an effective friction factor for oil-water flow is proposed.Employing the proposed correlations,the pressure gradient across the oil-water flow and hold-up volume fraction are predicted with significant reduction in error compared with that of conventionally employed correlations.The average error and standard deviation values of−7.06%,20.72%and 0.31%,18.79%are found for stratified flow and dispersed flow respectively.展开更多
The time-dependent liquid film thickness and pressure drop are measured by using parallel-wire conduc tance probes and capacitance differential-pressure transducer. A mathematical model with iterative procedure to cal...The time-dependent liquid film thickness and pressure drop are measured by using parallel-wire conduc tance probes and capacitance differential-pressure transducer. A mathematical model with iterative procedure to calculate holdup and pressure drop in horizontal and inclined gas-liquid stratified flow is developed. The predictions agree well with over a hundred experimental data in 0.024 and 0.04 m diameter pipelines.展开更多
为了研究不同堆积结构颗粒床内的流动特性,使用两种尺寸球形颗粒构建了均匀混合堆积结构和分层堆积结构床,在碎片床冷却性实验装置(DEBECO,DEbris BEd COolability)上进行了单相和两相流动实验。基于实验结果,对比分析了两种堆积结构的...为了研究不同堆积结构颗粒床内的流动特性,使用两种尺寸球形颗粒构建了均匀混合堆积结构和分层堆积结构床,在碎片床冷却性实验装置(DEBECO,DEbris BEd COolability)上进行了单相和两相流动实验。基于实验结果,对比分析了两种堆积结构的流动阻力压降,进一步验证了流动阻力模型。实验结果表明:对于不同尺寸颗粒均匀混合的堆积颗粒床,其有效直径在低速(Rep<7)条件下更接近面积平均直径;随着速度(Rep>7)升高,其有效直径更接近长度平均直径。当气液两相同向向上流过均匀堆积结构颗粒床时,实验测量的两相压降总体上与Reed模型预测值较为接近;与均匀堆积结构床相比,相同颗粒分层堆积结构床内的两相流动阻力压降较低。该实验研究结果对完善多孔介质结构内流动阻力分析具有重要的学术意义。展开更多
文摘The time-dependent liquid film thickness and pressure drop were measured by using parallel-wire conductance probes and capacitance differential-pressure transducers. Applying the eddy viscosity theory and an appropriate correlation of interfacial sear stress,a new two-dimensional separated model of holdup and pressure drop of turbulent/turbulent gas-liquid stratified flow was presented. Prediction results agreed well with experimental data.
文摘This paper aims to propose correlations to predict pressure gradient,friction factor and fluid phase hold-up in liquid-liquid horizontal pipe flow.To develop the correlations,experiments are conducted using high viscous oils(202 and 630 mPa⋅s)in a steel pipe of length 11.25 m and length-to-diameter ratio of 708.In addition,the experimental data from the literature comprising wide range of flow and fluid properties is analyzed.For the analysis,the liquid-liquid pipe flow data is categorized into two as:stratified and dispersed.The existing friction factor correlations are modified to incorporate the effects of viscosity of the oil phase,interfacial curvature(contact/wetting angle-in lieu of material of the pipe)and fluid phase fraction.In the two-fluid model of stratified flow,the wall stress and interfacial stress correlations are substituted with superficial velocities of fluids and superficial Reynolds numbers of fluid phases replacing fluid phase velocities and fluid Reynolds numbers.Similarly,for dispersed flow,an effective Reynolds number is described as the sum of superficial Reynolds number of oil and water phases.Substituting the generally employed mean or mixture Reynolds number with the effective Reynolds number into the existing single-phase turbulent flow friction factor correlation,an effective friction factor for oil-water flow is proposed.Employing the proposed correlations,the pressure gradient across the oil-water flow and hold-up volume fraction are predicted with significant reduction in error compared with that of conventionally employed correlations.The average error and standard deviation values of−7.06%,20.72%and 0.31%,18.79%are found for stratified flow and dispersed flow respectively.
文摘The time-dependent liquid film thickness and pressure drop are measured by using parallel-wire conduc tance probes and capacitance differential-pressure transducer. A mathematical model with iterative procedure to calculate holdup and pressure drop in horizontal and inclined gas-liquid stratified flow is developed. The predictions agree well with over a hundred experimental data in 0.024 and 0.04 m diameter pipelines.
文摘为了研究不同堆积结构颗粒床内的流动特性,使用两种尺寸球形颗粒构建了均匀混合堆积结构和分层堆积结构床,在碎片床冷却性实验装置(DEBECO,DEbris BEd COolability)上进行了单相和两相流动实验。基于实验结果,对比分析了两种堆积结构的流动阻力压降,进一步验证了流动阻力模型。实验结果表明:对于不同尺寸颗粒均匀混合的堆积颗粒床,其有效直径在低速(Rep<7)条件下更接近面积平均直径;随着速度(Rep>7)升高,其有效直径更接近长度平均直径。当气液两相同向向上流过均匀堆积结构颗粒床时,实验测量的两相压降总体上与Reed模型预测值较为接近;与均匀堆积结构床相比,相同颗粒分层堆积结构床内的两相流动阻力压降较低。该实验研究结果对完善多孔介质结构内流动阻力分析具有重要的学术意义。
