2018
DOI: 10.1002/cjce.23326
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CFD simulation of annular oil flow wrapped with water

Abstract: The transport of heavy oil in tubes is energy intensive since the oil viscosity can reach values of 10 500 000 cP. This study focuses on the transport of oil in a piping system by an annular flow of oil wrapped with water, since this alternative reduces head loss. The piping system was comprised of horizontal tubes, curves, and vertical tubes. The assumptions for the CFD simulation were the following: 3D geometry, turbulent flow, and isothermal system as well as incompressible, steady‐state, and transient flow… Show more

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Cited by 6 publications
(4 citation statements)
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“…The computational fluid dynamics (CFD) is the numerical branch of fluid mechanics. The basic equations of mass, momentum, and energy balances are differential equations that may mathematically represent, through the models, a huge number of physical phenomena, such as multiphase flows [27], reactive flows [28,29], and industrial equipment [30].…”
Section: Computational Fluid Dynamicsmentioning
confidence: 99%
“…The computational fluid dynamics (CFD) is the numerical branch of fluid mechanics. The basic equations of mass, momentum, and energy balances are differential equations that may mathematically represent, through the models, a huge number of physical phenomena, such as multiphase flows [27], reactive flows [28,29], and industrial equipment [30].…”
Section: Computational Fluid Dynamicsmentioning
confidence: 99%
“…Piping, which is widely used on an industrial level, may be considerably reduced for the transport of viscous fluids through simple adaptations during the design phase [4][5][6]. Core annular flow (CAF) is a promising solution from this point of view due to the lubricating effect of the adjacent water film on the wall [7][8][9][10]. Indeed, the contact of water with the wall leads to a drop in pressure [11].…”
Section: Introductionmentioning
confidence: 99%
“…Multiphase flow was an important theme in this special section with applications for oil transport, liquid‐liquid dispersion, flashing spray jets, solid‐fluid systems in rotating drums, trickle bed, and fluidized bed reactors, and agglomeration in cyclone separators . Mixing phenomena were reported in variety of geometries and on diverse length scales: in an agitated tubular reactor, in T‐shaped micromixers, and in fluidic oscillators .…”
mentioning
confidence: 99%