scholarly journals Pressure drop, flow pattern and local water volume fraction measurements of oil–water flow in pipes

2009 ◽  
Vol 20 (11) ◽  
pp. 114004 ◽  
Author(s):  
W A S Kumara ◽  
B M Halvorsen ◽  
M C Melaaen
2020 ◽  
Vol 12 (2) ◽  
pp. 173-180
Author(s):  
Anshumaan Dey ◽  
Monisha M. Mandal

The present numerical study is an effort to examine the hydrodynamics characteristics of two immiscible liquids (oil and water) flowing in different tubes. i.e., straight, coiled and Coiled Flow Inverter (CFI) tube of equal dimensions. CFI is a novel device in which fluid flow inversion takes place at uniform interval length of tube. The effect of oil-water viscosity ratio (µoil/µwater = 1.6 and 30) on velocity contours, phase distribution and pressure drop in the different tubes were investigated. The present work show that flow pattern of oil–water flows was changed from stratified to annular flows at higher water volume fraction for µoil/µwater = 1.6 in CFI. Phase inversion of oil–water flow was observed in CFI at higher viscosity ratio (µoil/µwater = 30). There was remarkable reduction in pressure drop with the increment in volume fraction of water flowing in coiled as well as CFI. CFI being more compact can be efficiently used in industries as chemical reactor, heat exchanger, mixer, etc.


2020 ◽  
Vol 15 (1) ◽  
pp. 1-7
Author(s):  
A. Abubakar

The need to ensure qualitative and reliable measurement of pressure drop of the oil-water flow cannot be over emphasized. In this regard, this study focused on the investigation of uncertainty in the measurement of pressure drop of oil-water flow in different acrylic pipe inclinations (0, +5ᴼ, +10ᴼ and -5ᴼ) and diameters (30.6-, 55.7- and 74.7-mm ID). The working fluids were tap water and mineral-based hydraulic oil (Shell Tellus S2 V 15), with medium viscosity and density of 24 cP and 872 kgm-3 respectively while the interfacial tension between the water and the oil was 12.9 mN/m at 25 ᴼC. The selected flow conditions were 0.5 and 1.0 m/s mixture velocities each at 0.1, 0.5 and 0.9 input water volume fractions. The repeatability, accuracy of the pressure transmitter, flow rate of the oil-water mixture and holdup (particularly for the inclined flow) were the sources of errors in the measurement of the pressure drop. The results showed that the average relative uncertainties in the pressure drop in 30.6-mm ID pipe were ±4.6 %, ±10.8 %, ±11.2 % and ±10.8 % in the 0ᴼ, +5ᴼ, +10ᴼ and -5ᴼ inclined flows respectively. Similarly, the average relative uncertainties in the pressure drop in the horizontal 55.7-mm and 74.7-mm ID pipes were ±5.7 % and ±7.5 % respectively. The largest contribution to the uncertainty in the pressure drop came from the flow rate and water holdup in the horizontal and inclined pipes respectively. The least contribution in both  horizontal and inclined pipes came from the accuracy of the pressure transmitter. Key words: Oil-water flow; Pressure drops; Standard uncertainty, Combined standard uncertainty; Expanded uncertainty


2000 ◽  
Vol 122 (4) ◽  
pp. 169-176 ◽  
Author(s):  
Yuri V. Fairuzov ◽  
Pedro Arenas-Medina ◽  
Jorge Verdejo-Fierro ◽  
Ruben Gonzalez-Islas

Full-scale experiments were conducted in order to investigate flow pattern transitions in horizontal pipelines carrying oil-water mixtures. In the experiments, a 16-in. pipeline conveying light crude oil was used. The line was connected to a freshwater network to control the input water volume fraction. A gate valve installed at the pipeline inlet controlled the oil flow rate. The transition from stratified flow to dispersed flow was determined by measuring the transversal water fraction profile. For this purpose, a special device, the multi-point sampling probe, was designed and installed into the pipeline. The probe has movable sampling tubes that allow taking samples simultaneously at six points along the diameter of the pipe. The rate of withdrawal of each sample was adjusted by a needle valve according to the mixture velocity in order to minimize the effect of the probe on the measured water fraction profile. The samples were analyzed for water content in a laboratory using a standard method for determining the water fraction in crude oils. Based on the data obtained, a flow pattern map was constructed. The experimental stratified/nonstratified transition boundary was compared with two theoretical criteria obtained in the linear stability analysis of stratified two-phase liquid-liquid flow. The results of this study can be useful for the design and operation of pipelines transporting crude oil, as well as for the validation of multifield multidimensional models of two-phase flow. [S0195-0738(00)00404-0]


Author(s):  
Elionora A. Caldera ◽  
Miguel Asuaje

In recent years, the oil sector has been struggling with the amount of water produced associated with the total volume of oil production. This quantity is known as water cut and could be over 90% in oil extraction. Handling of this water generates additional costs, affecting the sector’s revenues. In order to solve this problem, several techniques to reduce water cut in the wellbore have been applied. This paper evaluates CFD (computational fluid dynamics) models to predict phase segregation in dispersed oil in water flows. This evaluation has been conducted in an attempt to use CFD models to improve the design methodology of an inline separator of oil-water flow for petroleum production systems [1]. In this 3D study, three cases simulating water dominated dispersed oil-water flow in an inclined pipe 45° from horizontal, were evaluated numerically using a CFD model The oil was considered as the disperse phase and the water as the continuous phase, using Ansys®CFX. Mono size droplet dispersion was employed to represent the dispersed phase. The equations for the forces considered in this study are: drag and buoyancy. The simulated results are compared with the experimental data, which includes water volume fraction, drop pressure and separation efficiency. The result shows an improvement of over 50% in the experimental values, which match the values of the total flow rate (Q), water holdup (Hw) and pressure drop (ΔP), deviating by less than 4%.


2015 ◽  
Vol 73 ◽  
pp. 90-96 ◽  
Author(s):  
A. Mukhaimer ◽  
A. Al-Sarkhi ◽  
M. El Nakla ◽  
W.H. Ahmed ◽  
L. Al-Hadhrami

2009 ◽  
Vol 21 (1-2) ◽  
pp. 25-35
Author(s):  
Christophe Conan ◽  
Sandrine Decarre ◽  
Olivier Masbernat ◽  
Alain Line

2012 ◽  
Vol 625 ◽  
pp. 41-44
Author(s):  
Chao Sun ◽  
Qing Du ◽  
Yan Yin ◽  
Bin Jia

The performance of proton exchange membrane fuel cell is greatly influenced by the presence, distribution and transport of liquid water in the gas diffusion layer (GDL). In this study, air-water flow in a 3D GDL microstructure along the in-plane direction is studied numerically by using the volume of fluid (VOF) method. The GDL microstructure is considered initially filled with water, air flows into the structure under the driving force of a set pressure drop and the flow is supported by the capillary pressure due to the hydrophobic nature of the GDL structure. It is found that water removal can be accelerated by improving pressure drop. Pressure drop has little influence on the state-steady water volume fraction when the pressure drop is over a critical value.


2015 ◽  
Vol 128 ◽  
pp. 145-149 ◽  
Author(s):  
A. Mukhaimer ◽  
A. Al-Sarkhi ◽  
M. El Nakla ◽  
W.H. Ahmed ◽  
L. Al-Hadhrami

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