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Predicting liquid gradient in a pumping-well annulus

Journal Article · · SPE (Society of Petroleum Engineers) Product. Eng.; (United States)
DOI:https://doi.org/10.2118/13638-PA· OSTI ID:7053099

This work proposes a hydrodynamic model for estimating gas void fraction, f/sub g/, in the bubbly and slug flow regimes. The model is developed from experimental work, involving an air/water system, and from theoretical arguments. The proposed model suggests that prediction of f/sub g/, and hence the bottomhole pressure (BHP), is dependent on such variables as tubing-to-casing-diameter ratio, densities of gas and liquid, and surface tension. Available correlations do not include these variables as flexible inputs for a given system. Computation on a field example indicates that slug flow is the most dominant flow mechanism near the top of liquid column at the earliest times of a buildup test. As buildup progresses, transition from slug to bubbly flow occurs in the entire liquid column. Beyond the afterflow-dominated period, the effect of bubbly flow diminishes as gas flow becomes negligibly small. Comparisons of BHP's are made with the proposed and available correlations. Because the proposed model predicts f/sub g/ between these of the Godbey-Dimon and Podio et al. correlations, BHP is predicted accordingly.

Research Organization:
Univ. of North Dakota (US)
OSTI ID:
7053099
Journal Information:
SPE (Society of Petroleum Engineers) Product. Eng.; (United States), Journal Name: SPE (Society of Petroleum Engineers) Product. Eng.; (United States) Vol. 3:1; ISSN SPENE
Country of Publication:
United States
Language:
English

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