Computational fluid dynamics (CFD) analysis was performed in four different 90 degree elbows with air-water two-phase flows. The inside diameters of the elbows were 6.35?mm and 12.7?mm with radius to diameter ratios ( ) of 1.5 to 3. The pressure drops at two different upstream and downstream locations were investigated using empirical, experimental, and computational methods. The combination of three different air velocities, ranging from 15.24 to 45.72?m/sec, and nine different water velocities, in the range of 0.1–10.0?m/s, was used in this study. CFD analysis was performed using the mixture model and a commercial code, FLUENT. The comparison of CFD predictions with experimental data and empirical model outputs showed good agreement. 1. Introduction and Background In most industrial processes, fluids are used as a medium for material transport. A complete knowledge of the principles that rule the phenomena involving fluids transportation leads to more efficient and secure systems. However, in many industries, such as petroleum, chemical, oil, and gas industries, two-phase or multiphase flow is frequently observed [1]. Multiphase flow is defined as the simultaneous flow of several phases, with the simplest case being a two-phase flow [2]. Compared to single-phase flow, the equations associated with two-phase flow are very complex, due to the presence of different flow patterns in gas-liquid systems [3]. A detailed discussion of two-phase flow phenomenon behavior is provided by Wallis [2]. The flow patterns observed in horizontal flow are bubble, stratified, stratified wavy, slug, and annular. In vertical flows, bubble, plug, slug (or churn), annular, and wispy-annular flow patterns are present. Several investigations have been reported to determine the friction factor and pressure drops in horizontal [4] and vertical [5] two-phase and multiphase flows [6]. The presence of the two-phase flow typically produces an undesirable higher-pressure drop in the piping components. In most industrial installations, elbows are frequently used to direct the flow and provide flexibility to the system [7]. Since these fittings are also used to install instruments that monitor the main parameters of the industrial process, it is important to have a reliable way to evaluate the pressure drop in these elbows [8]. As the fluid flows through the bend, the curvature of bend causes a centrifugal force; the centrifugal force is directed toward the outer wall of the pipe from the momentary center of the curvature. The combined presence of centrifugal force and boundary layer
References
[1]
S. F. Sánchez, R. J. C. Luna, M. I. Carvajal, and E. Tolentino:, “Pressure drop models evaluation for two-phase flow in 90 degree horizontal elbows,” Ingenieria Mecanica Techilogia Y Desarrollo, vol. 3, no. 4, pp. 115–122, 2010.
[2]
G. B. Wallis, One Dimensional Two-Phase Flow, McGraw-Hill, 1969.
[3]
S. Benbella, M. Al-Shannag, and Z. A. Al-Anber, “Gas-liquid pressure drop in vertical internally wavy 90° bend,” Experimental Thermal and Fluid Science, vol. 33, no. 2, pp. 340–347, 2009.
[4]
J. S. Cole, G. F. Donnelly, and P. L. Spedding, “Friction factors in two phase horizontal pipe flow,” International Communications in Heat and Mass Transfer, vol. 31, no. 7, pp. 909–917, 2004.
[5]
S. Wongwises and W. Kongkiatwanitch, “Interfacial friction factor in vertical upward gas-liquid annular two-phase flow,” International Communications in Heat and Mass Transfer, vol. 28, no. 3, pp. 323–336, 2001.
[6]
P. L. Spedding, E. Benard, and G. F. Donnelly, “Prediction of pressure drop in multiphase horizontal pipe flow,” International Communications in Heat and Mass Transfer, vol. 33, no. 9, pp. 1053–1062, 2006.
[7]
J. Hernández Ruíz, Estudio del comportamiento de flujo de fluidos en tuberías curvas para plicaciones en metrología [Tesis de Maestría], IPN-ESIME, 1998.
[8]
A. M. Chan, K. J. Maynard, J. Ramundi, and E. Wiklund, “Qualifying elbow meters for high pressure flow measurements in an operating nuclear power plant,” in Proceedings of the 14th International Conference on Nuclear Engineering (ICONE '06), Miami, Fla, USA, July 2006.
[9]
A. Azzi and L. Friedel, “Two-phase upward flow 90° bend pressure loss model,” Forschung im Ingenieurwesen, vol. 69, no. 2, pp. 120–130, 2005.
[10]
D. Chisholm, Two-Phase Flow in Pipelines and Heat Exchangers, Godwin, 1983.
[11]
J. M. Chenoweth and M. W. Martin, “Turbulent two-phase flow,” Petroleum Refiner, vol. 34, no. 10, pp. 151–155, 1955.
[12]
R. W. Lockhart and R. C. Martinelli, “Proposed correlation of data for isothermal two-phase two-component flow in pipes,” Chemical Engineering Progress, vol. 45, no. 1, pp. 39–48, 1949.
[13]
P. E. Fitzsimmons, “Two phase pressure drop in pipe components,” Tech. Rep. HW-80970 Rev 1, General Electric Research, 1964.
[14]
K. Sekoda, Y. Sato, and S. Kariya, “Horizontal two-phase air-water flow characteristics in the disturbed region due to a 90-degree bend,” Japan Society Mechanical Engineering, vol. 35, no. 289, pp. 2227–2333, 1969.
[15]
A. Asghar, R. Masoud, S. Jafar, and A. A. Ammar, “CFD and artificial neural network modeling of two-phase flow pressure drop,” International Communications in Heat and Mass Transfer, vol. 36, no. 8, pp. 850–856, 2009.
[16]
T. L. Deobold, “An experimental investigation of two-phase pressure losses in pipe elbows,” Tech. Rep. HW-SA, 2564, MSc. University of Idaho, Chemical Engineering, 1962.
[17]
G. E. Alves, “Co-current liquid-gas flow in a pipe-line contactor,” Chemical Engineering Progress, vol. 50, no. 9, pp. 449–456, 1954.
[18]
M. A. Peshkin, “About the hydraulic resistance of pipe bends to the flow of gas-liquid mixtures,” Teploenergetika, vol. 8, no. 6, pp. 79–80, 1961.
[19]
S. S. Kutateladze, Problems of Heat Transfer and Hydraulics of Two-Phase Media, Pergamon Press, Oxford, UK.
[20]
S. F. Moujaes and S. Aekula, “CFD predictions and experimental comparisons of pressure drop effects of turning vanes in 90° duct elbows,” Journal of Energy Engineering, vol. 135, no. 4, pp. 119–126, 2009.
[21]
Q. H. Mazumder, S. A. Shirazi, and B. S. McLaury, “Prediction of solid particle erosive wear of elbows in multiphase annular flow-model development and experimental validation,” Journal of Energy Resources Technology, vol. 130, no. 2, Article ID 023001, 10 pages, 2008.
[22]
I. Fluent, Fluent 6. 3 User Guide, Fluent Inc., Lebanon, NH, USA, 2002.
[23]
N. P. Cheremisinoff, Ed., Encyclopedia of Fluid Mechanics: Gas Liquid Flows, vol. 3, Gulf Publishing Company, 1986.
[24]
S. W. Churchill, “Friction equation spans all fluid flow regimes,” Chemical Engineering, vol. 84, no. 24, pp. 91–92, 1977.