Abstract
The effect of surface choking on gaslift stability and flow regime transition in vertical cylindrical pipe during gaslift operation is investigated. Here, a laboratory scale multiphase flow rig was designed, fabricated, and assembled. Gas rates of 0.000113 m3/s and 0.000187 m3/s were imposed on a 1 mm single nozzle injector. Surface choking was implemented by setting the system to 15%, 25%, 50% and 100% opening. For each opening condition, transient pressure at four locations; corresponding to length-to-diameter ratios of 0.0, 18.3, 36.7, and 53.3, was recorded. Flow structure and regime transition are characterised by visual, photographic and slow-motion videos, recorded at each location. A transition from random peak-to-peak cyclic and periodic pressure oscillation, accompanied by pressure increase, is observed. Further, bubble size reduction characterised by low vorticity and turbulence is observed at 15% opening. It is concluded that surface choking must be complemented by knowledge of flow behaviour within the system.
Original language | English |
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Pages (from-to) | 258-278 |
Number of pages | 22 |
Journal | International Journal of Oil, Gas and Coal Technology |
Volume | 35 |
Issue number | 3 |
Early online date | 5 Apr 2024 |
DOIs | |
Publication status | Published - 5 Apr 2024 |
Bibliographical note
AcknowledgementsThe authors wish to thank the financial support provided by the University of Aberdeen scholarship awarding section for sponsoring this project.
Keywords
- Gas-lift
- Multiphase flow
- Instability
- Fluid Flow Structure