Upscaling modeling using dimensional analysis in gas–liquid annular and stratified flows

Al–Sarkhi, A.; Duc, V. N.; Sarica, Cem; Pereryra, E.

doi:10.1016/j.petrol.2015.11.028

Cited by 9 publications

(1 citation statement)

References 6 publications

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“…Dimensionless numbers are often applied to characterize flow similarity in different situations when modeling flow behavior, which means different flow situations can be simulated similarly if proper dimensionless numbers are selected. Some scholars [31][32][33] have proposed new dimensionless numbers based on the modified Froude number in stratified and annular flows, and achieved high accuracy. The gas/liquid dimensionless numbers can be given as follows:…”

Section: Test Matrixmentioning

confidence: 99%

Effect of Lateral Trajectory on Two-Phase Flow in Horizontal Shale Gas Wells

Yang,

Chen,

Peng

et al. 2023

Processes

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Horizontal gas wells are one of the key technologies for the production of shale gas reservoirs. Compared with conventional gas reservoirs, horizontal shale gas wells have ultra-long and complex lateral sections. Overall, toe-up, toe-down, and horizontal trajectories will be exhibited in the lateral section. The statistical results of field production data indicate that the lateral trajectory has a significant impact on the estimated ultimate recovery. However, the mechanism has not yet been fully revealed owing to the complicated two-phase flow in lateral pipes. Therefore, taking horizontal shale gas wells’ lateral section as the research object, we designed our experimental parameter ranges based on horizontal shale gas wells in the Changning shale gas field. Simulation experimental tests were conducted on the pipe with an inclined angle from −15° to 15° to analyze the effects of different gas velocities, liquid velocities, and pipe inclinations on flow patterns and liquid holdup. Based on our observations and measurements, we evaluated the flow pattern prediction methods and drew a new flow pattern map for pipes with an inclined angle from −15° to 15°. Based on the momentum conservations between the gas and liquid phases and measured liquid holdup data, a new liquid holdup model was established in the pipes with inclined angle from −15° to 15°. Experimental and field-measured data were collected to verify the new method’s accuracy.

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Section: Test Matrixmentioning

confidence: 99%