Phase split of nitrogen/non-Newtonian fluid two-phase flow at a micro-T-junction

Abstract An experimental investigation has been undertaken to understand the phase split of nitrogen gas/non-Newtonian liquid two-phase flow passing through a 0.5 mm T-junction that oriented horizontally. Four different liquids, including water and aqueous solutions of carboxymethyl cellulose (CMC) with different mass concentrations of 0.1, 0.2 and 0.3 wt%, were employed. Rheology experiments showed that different from water, CMC solutions in this study are pseudoplastic non-Newtonian fluid whose viscosity decreases with increasing the shear rate. The inlet flow patterns were observed to be slug flow, slug–annular flow and annular flow. The fraction of liquid taken off at the side arm for nitrogen gas/non-Newtonian liquid systems is found to be higher than that for nitrogen gas/Newtonian liquid systems in all inlet flow patterns. In addition, with increasing the pseudoplasticity of the liquid phase, the side arm liquid taken off increases, but the increasing degree varies with each flow pattern. For annular flow, the increasing degree is much greater than those for slug and slug–annular flows.

[1]  Kui He,et al.  Phase splitting of a slug–annular flow at a horizontal micro-T-junction , 2011 .

[2]  H. M. Soliman,et al.  Two-phase flow in a horizontal equal-sided impacting tee junction , 2007 .

[3]  Masahiro Shoji,et al.  Fluctuation characteristics of two-phase flow splitting at a vertical impacting T-junction , 2002 .

[4]  Ovadia Shoham,et al.  Two-phase flow splitting in a tee junction—experiment and modelling , 1987 .

[5]  Barry J. Azzopardi,et al.  Affecting the phase split at a large diameter T-junction by using baffles , 2004 .

[6]  Barry J. Azzopardi,et al.  Slug flow in small diameter pipes and T-junctions , 2005 .

[7]  Keumnam Cho,et al.  Two-phase split of refrigerants at a T-junction , 2006 .

[8]  Masahiro Kawaji,et al.  The effect of channel diameter on adiabatic two-phase flow characteristics in microchannels ☆ , 2004 .

[9]  Barry J. Azzopardi,et al.  The split of horizontal annular flow at a T-junction , 1997 .

[10]  B. Liu,et al.  Nitrogen/non-Newtonian fluid two-phase upward flow in non-circular microchannels , 2010 .

[11]  Liu Qi,et al.  Gas-liquid two-phase flow division at a micro-T-junction , 2010 .

[12]  Corrado Schenone,et al.  Experiments on two-phase flow distribution inside parallel channels of compact heat exchangers , 2008 .

[13]  Barry J. Azzopardi,et al.  Plant Application of a T-Junction as a Partial Phase Separator , 2002 .

[14]  Philipp Rudolf von Rohr,et al.  Two-phase flow characteristics in gas–liquid microreactors , 2006 .

[15]  Barry J. Azzopardi,et al.  The split of annular two-phase flow at a small diameter T-junction , 2000 .

[16]  B. J. Azzopardi The effect of the side arm diameter on the two-phase flow split at a «T» junction , 1984 .

[17]  B. J. Azzopardi,et al.  The effect of flow patterns on two-phase flow in a T junction , 1982 .

[18]  M. Dziubiński,et al.  The flow pattern map of a two-phase non-Newtonian liquid–gas flow in the vertical pipe , 2004 .

[19]  Said I. Abdel-Khalik,et al.  Gas–liquid two-phase flow in microchannels Part I: two-phase flow patterns , 1999 .

[20]  Barry J. Azzopardi,et al.  Transient effects in gas–liquid phase separation at a pair of T-junctions , 2008 .

[21]  Dionissios P. Margaris,et al.  T-junction separation modelling in gas–liquid two-phase flow , 2007 .

[22]  Richard T. Lahey,et al.  Phase separation in dividing two-phase flows , 1988 .

[23]  David F. Fletcher,et al.  Film and slug behaviour in intermittent slug–annular microchannel flows , 2010 .

[24]  K. C. Hong Two-Phase Flow Splitting at a Pipe Tee , 1978 .