Single-Phase and Two-Phase Flow Through Thin and Thick Orifices in Horizontal Pipes

被引:41
作者
Roul, Manmatha K. [1 ]
Dash, Sukanta K. [2 ]
机构
[1] Bhadrak Inst Engn & Technol, Dept Mech Engn, Bhadrak 756113, India
[2] Indian Inst Technol, Dept Mech Engn, Kharagpur 721302, W Bengal, India
来源
JOURNAL OF FLUIDS ENGINEERING-TRANSACTIONS OF THE ASME | 2012年 / 134卷 / 09期
关键词
GAS-LIQUID FLOW; PRESSURE-DROP; MODEL;
D O I
10.1115/1.4007267
中图分类号
TH [机械、仪表工业];
学科分类号
0802 ;
摘要
Two-phase flow pressure drops through thin and thick orifices have been numerically investigated with air-water flows in horizontal pipes. Two-phase computational fluid dynamics (CFD) calculations, using the Eulerian-Eulerian model have been employed to calculate the pressure drop through orifices. The operating conditions cover the gas and liquid superficial velocity ranges V-sg = 0.3-4 m/s and V-sl = 0.6-2 m/s, respectively. The local pressure drops have been obtained by means of extrapolation from the computed upstream and downstream linearized pressure profiles to the orifice section. Simulations for the single-phase flow of water have been carried out for local liquid Reynolds number (Re based on orifice diameter) ranging from 3 x 10(4) to 2 x 10(5) to obtain the discharge coefficient and the two-phase local multiplier, which when multiplied with the pressure drop of water (for same mass flow of water and two phase mixture) will reproduce the pressure drop for two phase flow through the orifice. The effect of orifice geometry on two-phase pressure losses has been considered by selecting two pipes of 60mm and 40mm inner diameter and eight different orifice plates (for each pipe) with two area ratios (sigma = 0.73 and sigma = 0.54) and four different thicknesses (s/d = 0.025-0.59). The results obtained from numerical simulations are validated against experimental data from the literature and are found to be in good agreement. [DOI: 10.1115/1.4007267]
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页数:14
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