0
Research Papers: Flows in Complex Systems

Flow Pattern and Slug Dynamics Around a Flow Splitter

[+] Author and Article Information
M. B. Alamu

 Floxpat Petroleum and Energy Service LTD., Suite 16418, Lower Ground Floor, 145-157 St John Street, EC1V 4PW, London, UKmhunir.alamu@floxpat.com

B. J. Azzopardi

Faculty of Engineering, Process and Environmental Engineering Division,  University of Nottingham, NG7 2RD, University Park, UK

J. Fluids Eng 133(12), 121105 (Dec 23, 2011) (9 pages) doi:10.1115/1.4005196 History: Received September 05, 2011; Revised September 20, 2011; Published December 23, 2011; Online December 23, 2011

Application of dividing junction in sub-sea separation of a hydrocarbon well stream is becoming increasingly popular across the petroleum industry. They are often used in stage separation of a hydrocarbon well stream to reduce process load on a primary separator. Where the diameters of the pipes making up the junction are small, it is of particular interest to nano multiphase flow technology (NMFT) currently being advocated. While there is a body of data for small diameter dividing junctions, it is almost exclusively for air-water where the pattern before flow and after the junction in the vertical segment of the pipe is usually unchanged. Here, new data for air and more viscous liquid are presented. They have been acquired from electrical resistance measurements made between pairs of flush-mounted ring conductance probes located around the junction. Liquid phase viscosities were varied systematically between 1 mPa·s (water) and 36 mPa·s (water-glycerol mixture). The implemented test matrix varied between 0 – 32 m/s for gas superficial velocity and 0.003 – 1.3 m/s for liquid superficial velocity respectively. The internal pipe diameter making up the junction is 5 mm. The time varying void fraction obtained has been used to obtain probability density functions (PDF) to characterize the flow. PDF exhibit lower peaks and a marked shift in the direction of decreasing void fraction for more viscous liquid. Flow structure frequency was extracted from a detailed spectrum analysis (PSD) based on the fluctuation of void wave signals with time. The result shows that the dominant frequency of the flow structure increases as liquid viscosity increases. Analysis of the measured phase split data reveals additional flow assurance details. This study shows the effect of liquid viscosity becomes significant only when the gas taken off exceeds a threshold of 0.40. The plot of the liquid hold-up against the mixture velocity fingerprints churn-annular transition boundary around a gas superficial velocity of 15 m/s. The flow pattern approaching the junction changes after leaving the junction in the vertical run arm as liquid viscosity increases; however, an increase in liquid viscosity has no effect on flow pattern in the horizontal side arm.

FIGURES IN THIS ARTICLE
<>
Copyright © 2011 by American Society of Mechanical Engineers
Your Session has timed out. Please sign back in to continue.

References

Figures

Grahic Jump Location
Figure 1

The flow diagram with T-junction test section

Grahic Jump Location
Figure 2

Calibration curves for the vertical conductance probes

Grahic Jump Location
Figure 3

Calibration of the horizontal conductance probes. Comparisons were made with previous works.

Grahic Jump Location
Figure 4

Cross sectional view of the ring type conductance probe

Grahic Jump Location
Figure 5

Time averaged void fraction for air-water and air-glycerol solution. Gas superficial velocity = 3.2 m/s, liquid superficial velocity = 0.12 m/s, Liquid viscosity = 36.0 mPa·s, Gas Take Off = 0.68, Liquid Take Off = 0.68.

Grahic Jump Location
Figure 6

Effect of gas superficial velocity on liquid hold-up showing transition to annular flow

Grahic Jump Location
Figure 7

Present data represented on flow pattern map of Taitel [13]

Grahic Jump Location
Figure 8

Comparison of air-water and air-viscous liquid data at the same flow conditions using liquid hold-up and PDF of void fraction. Gas superficial velocity = 3.2 m/s, liquid superficial velocity = 0.12 m/s. T-junction Pressure = 1.4 bar. Gas Take Off = 0.68; Liquid Take Off = 0.68.

Grahic Jump Location
Figure 9

Comparison of water and more viscous phase split data for gas superficial velocity of 15 m/s and liquid superficial velocity of 0.10 m/s

Grahic Jump Location
Figure 10

Effect of liquid physical properties on phase split at fixed superficial liquid velocity of 0.1 m/s

Grahic Jump Location
Figure 11

Variation of structure frequency around the junction

Grahic Jump Location
Figure 12

Structure frequency at side arm and main pipe as a function of structure frequency approaching the junction. 1 refers to the inlet pipe, 2 to the straight through continuation and 3 to the side arm respectively.

Tables

Errata

Discussions

Some tools below are only available to our subscribers or users with an online account.

Related Content

Customize your page view by dragging and repositioning the boxes below.

Related Journal Articles
Related eBook Content
Topic Collections

Sorry! You do not have access to this content. For assistance or to subscribe, please contact us:

  • TELEPHONE: 1-800-843-2763 (Toll-free in the USA)
  • EMAIL: asmedigitalcollection@asme.org
Sign In