Non-Newtonian Liquid-Gas Non-Uniform Stratified Flow With Interfacial Level Gradient Through Horizontal Tubes

Author:

Li Haiwang12,Neng Wong Teck3,Skote Martin,Duan Fei1

Affiliation:

1. School of Mechanical and Aerospace Engineering, Nanyang Technological University, 50 Nanyang Avenue, Singapore 639798

2. National Key Lab. of Science and Technology on Aero-Engines, Beijing University of Aeronautics and Astronautics, Beijing 100191, China

3. e-mail:

Abstract

This paper presents the predictions of the axial distribution of liquid level and interfacial level gradient (ILG) for nonuniform non-Newtonian liquid-gas flow in horizontal tubes. The non-Newtonian liquid is described using power-law model, while the model of Heywood and Charles for uniform non-Newtonian liquid-gas two-phase flow, which was developed based on one dimensional energy equation, is extended to describe nonuniform stratified flow by incorporating the effect of interfacial level gradient. Two different critical liquid levels are found from the energy equation and are adopted as boundary condition to calculate the interfacial level distribution upstream of the channel exit. The results from the model are compared with the published numerical and experimental data. The results show that the model can predict the interfacial level distribution and interfacial level gradient for nonuniform stratified flow. Low liquid velocity, low gas velocity and high liquid viscosity are beneficial for forming a nonuniform flow with interfacial level gradient. The difference between the analytical model and the published data is smaller than 10%.

Publisher

ASME International

Subject

Mechanical Engineering

Reference22 articles.

1. Numerical Analysis of Viscoelastic Fluids in Steady Pressure-Driven Channel Flow;ASME Trans. J. Fluids Eng.,2012

2. Co-Current Gas-Liquid Smooth-Stratified Flow in a Horizontal Reduced t-Junction Including Wavy and Slug Regime Transition Boundaries;ASME Trans. J. Fluids Eng.,2011

3. Analysis of Multi-Layer Immiscible Fluid Flow in a Microchannel;ASME Trans. J. Fluids Eng.,2011

4. Exact Solution of Two Phase Stratified Flow Through the Pipes for Non-Newtonian Herschel-Bulkley Fluids;Int. Commun. Heat Mass Transfer,2009

5. Gazley, C., 1948, “Interfacial Shear and Stability in Two-Phase Flow,” Ph.D. thesis, University of Delaware, Newark, NJ.

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