Effects of high oil viscosity on oil‐gas downward flow in deviated pipes. Part 1: Experimental setup and flow pattern transitions

Author(s):  
Gabriel Soto‐Cortes ◽  
Eduardo Pereyra ◽  
Cem Sarica ◽  
Fabian Rivera‐Trejo ◽  
Carlos Torres
Author(s):  
Gabriel Soto‐Cortes ◽  
Eduardo Pereyra ◽  
Cem Sarica ◽  
Fabian Rivera‐Trejo ◽  
Carlos Torres

2021 ◽  
pp. 1-24
Author(s):  
Marcel C. Barbosa ◽  
Oscar M. H. Rodriguez

Abstract Proper sizing of flow lines in the upstream energy industry depends on accurate modeling of gas-liquid flow, which has a common occurrence in production wells and has been studied thoroughly for many decades. However, data of flow in duct geometries different from circular pipes and when the liquid viscosity is much higher than that of water are scarce. Proper prediction of pressure gradient, heat and mass transfer and corrosion depends on the accuracy of the model used to calculate the volumetric phase fraction. In pumped directional wells with inverted-shroud gravitational separators there is flow through an annular duct formed between the wells' casing and the separator itself that can have some tens of meters. The present work is an investigation on upward vertical/inclined high-viscous-oil/gas flow in a large and narrow annulus (30mm hydraulic diameter with an outer diameter equal to 155mm), using a radial geometry comparable to those found in real production systems. Air-water and air-oil mixtures, the latter with two oil viscosity ranges, were used as working fluids. The experimental test section used was 9.67m long positioned at 90° (vertical) and 45° and made of two concentric pipes. Flow pattern transitions from the literature were analyzed and compared to the collected experimental data. Drift-flux parameters were obtained from multiple working conditions. These drift-flux parameters were employed in the development of a novel flow-pattern-independent correlation, compared against the present data and other data sets from the literature in which other geometries and fluids were used. The predictions of the proposed drift-flux correlation are significantly superior in comparison to correlations selected from the literature in all cases.


2011 ◽  
Vol 317-319 ◽  
pp. 2239-2243
Author(s):  
Yang Liu ◽  
Zhi Hua Wang ◽  
Li Xin Wei ◽  
Ren Shan Pang

The crude oil in Kuidong region of Liaohe Tanhai Oilfield is characterized by high oil viscosity, high density, high content of colloid asphalt, low content of wax and low freezing point. In the shallow region, the large current, high content of silt, long-distance subsea buried pipeline and drift ice in winter have brought great challenge to offshore construction and oil-gas transportation. In this paper, the investigations of offshore construction project and platform process are shown. Based on the well production rate, gas-oil ratio, water cut, wellhead back pressure and outlet temperature, the range of daily transportation volume was acquired, as well as the maximum inlet pressure and pressure difference of the pump. The paper also selected technically and economically feasible pumps, then designed the public projects, corresponding electric power and self-control facilities. The selected skidded twin screw multiphase pump system can smoothly transport produced liquid to the terminal systems onshore without any effect on the daily output.


2013 ◽  
Author(s):  
Xiaoyan Liu ◽  
Qianjun Mao ◽  
Lijun Liu ◽  
Ying Xu ◽  
Wei Chen
Keyword(s):  

Author(s):  
Lingzi Wang ◽  
Jianmei Feng ◽  
Shijing Xu ◽  
Xiang Gao ◽  
Xueyuan Peng

The film flow behavior in an oil–gas cyclone separator was experimentally studied to improve the separation efficiency in terms of the effect of the oil film on the cylinder wall. The oil film flow pattern was captured using a high-speed camera, and the cylinder wall was divided into seven regions to analyze according to the different oil film flow patterns. Along the cyclone cylinder height, the central part of the cylinder was the main flow area, in which droplet–wall collisions and oil film splashing were severe. Additionally, the oil film’s distribution characteristics under inlet velocities of 14.0, 16.0, and 18.0 m/s were compared, and the results showed that more splashing oil droplets were generated under higher inlet velocity. Moreover, changing the structure of the central channel and outer cylinder slightly changed the oil film’s area and flow pattern but exhibited a weak effect on the oil film thickness and re-entrainment. Then, an improved structure was proposed by adding a porous cylinder to the outer cyclone to avoid the generation of small splashing droplets from the oil film. The performance of the modified separator was measured in a real oil-injected compressor system, which demonstrated higher separation efficiency with no increase in static pressure loss. The separation efficiency increased by up to 2.7%, while the pressure loss decreased by up to 10%. Thus, the improved structure can improve the performance of oil–gas separators by changing the distribution and thickness of the oil film on the cylinder wall.


2010 ◽  
Vol 5 (3) ◽  
pp. 20-28
Author(s):  
Ilya D. Zverkov ◽  
Viktor V. Kozlov ◽  
Alexey V. Kryukov

Flow visualization for classical and “wavy” wings at low Reynolds number was carry out with thermovision camera. Some procedure details for such kind of investigation were specified. It was shown that thermovision as compared to classical flow visualization methods, make it possible to determine quite accurately, the flow features of interest. This makes the method very attractive at preliminary estimation of the flow pattern for its detailed investigation. The experimental setup and thermovision results are presented. A comparison between thermovision and oil-film visualization is conducted.


2008 ◽  
Vol 3 (02) ◽  
pp. 1-11 ◽  
Author(s):  
Bahadir Gokcal ◽  
Qian Wang ◽  
Hong-Quan Zhang ◽  
Cem Sarica

SPE Journal ◽  
2019 ◽  
Vol 24 (05) ◽  
pp. 2221-2238 ◽  
Author(s):  
Hendy T. Rodrigues ◽  
Eduardo Pereyra ◽  
Cem Sarica

Summary This paper studied the effects of system pressure on 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 were calculated 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–inside diameter (ID) pipe inclined at 2° from 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 does a traditional slug flow. 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 gravity–dominated. Pressure gradient is a function of FrSg and liquid superficial velocity, 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 showed a small variation in the stratified and annular flow patterns. Model comparison produced mixed results, depending on the specific flow conditions. A relation between the measured interfacial roughness and the interfacial friction factor was proposed, and the results agreed with the existing measurements.


2019 ◽  
Vol 109 ◽  
pp. 109896
Author(s):  
Gabriel Soto-Cortes ◽  
Eduardo Pereyra ◽  
Cem Sarica ◽  
Fabian Rivera-Trejo ◽  
Carlos Torres

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