Affiliation:
1. U. of North Dakota
2. Chevron Overseas Petroleum Technology Co.
Abstract
Summary
This paper presents the results of an experimental study and a semitheoretical analysis of two-phase oil/water flow in vertical and deviated systems. The study focuses on water-dominated flow regimes, where the patterns may be termed as bubbly flow, pseudoslug flow, and churn flow. A drift-flux approach is taken to analyze the flow behavior of oil/water systems. For the three flow regimes investigated, the drift velocity of the lighter oil phase is found to be dependent on its in-situ volume fraction in addition to the terminal bubble- or droplet-rise velocity. For flow in both vertical and deviated pipes, we were able to develop a single expression for the drift flux, uow, resulting in a single equation for the in-situ oil fraction, fo, for the three flow regimes studied. We correlated fo with the oil superficial velocity, vos, and the terminal rise velocity, vꝏθ, using the expression, fo=vos/{1.2vm + vꝏθ f(1 — fo)2}. In a deviated pipe, the terminal rise velocity, vꝏθ, is correlated with that in a vertical pipe by =vꝏ/'″ (cosθ)0.5(1 + sinθ)2, for θ <70°. The performance of the proposed method in estimating fo is in good agreement with our measurements. Published data further augment the approach presented here.
Publisher
Society of Petroleum Engineers (SPE)
Cited by
32 articles.
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