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    Experiment Research of Phase Inversion in Mineral Oil-Water Two-Phase Flow in Horizontal Pipe

    Source: Journal of Energy Resources Technology:;2009:;volume( 131 ):;issue: 004::page 43001
    Author:
    Wei Wang
    ,
    Jing Gong
    DOI: 10.1115/1.4000324
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: In oil-water two-phase dispersed flow, phase inversion may occur when the continuous phase becomes dispersed. This phenomenon, which controls the nature of the phase in contact with the pipe, has a great importance on the corrosion and on the pressure drop, which dramatically affects the delivery ability and operational modality. It is therefore imperative for the phase inversion research to be taken into consideration. However, most of the knowledge on phase inversion is for light mineral oil with low viscosity, few research focuses on high viscosity oil-water phase inversion. (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium , Oklahoma, SPE Paper No. 18836) found that critical water fraction when inversion occurred was dramatically reduced with the increment of oil viscosity, and the existing phase inversion models are invalidated. In this paper, an experimental study has been made of high viscosity mineral oil-water flow through a horizontal pipe loop. Results indicate that phase inversion for oil phase with high viscosity occurs much earlier than low viscosity oil, and phase inversion tends to be delayed, with the increment in experimental temperature. The influence of mixture velocities on the inversion process could be neglected in the range of mixture velocities that we studied. As well, inversion point obtain by our experiment are best predicted by the correlation of (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium , Oklahoma, SPE Paper No. 18836). Models of and (1997, “Phase Inversion Prediction Study,” Rev. Inst. Fr. Pet., 52, pp. 415–424) and and (2002, “Modeling of Phase Inversion Phenomenon in Two-Phase Pipe Flows,” Int. J. Multiph. Flow, 28, pp. 1177–1204), based on minimization of system total energy, seem to be invalidated for high viscosity oil.
    keyword(s): Pipes , Water , Flow (Dynamics) , Viscosity , Mixtures , Pressure drop AND Two-phase flow ,
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      Experiment Research of Phase Inversion in Mineral Oil-Water Two-Phase Flow in Horizontal Pipe

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    http://yetl.yabesh.ir/yetl1/handle/yetl/140344
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    contributor authorWei Wang
    contributor authorJing Gong
    date accessioned2017-05-09T00:32:24Z
    date available2017-05-09T00:32:24Z
    date copyrightDecember, 2009
    date issued2009
    identifier issn0195-0738
    identifier otherJERTD2-26566#043001_1.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/140344
    description abstractIn oil-water two-phase dispersed flow, phase inversion may occur when the continuous phase becomes dispersed. This phenomenon, which controls the nature of the phase in contact with the pipe, has a great importance on the corrosion and on the pressure drop, which dramatically affects the delivery ability and operational modality. It is therefore imperative for the phase inversion research to be taken into consideration. However, most of the knowledge on phase inversion is for light mineral oil with low viscosity, few research focuses on high viscosity oil-water phase inversion. (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium , Oklahoma, SPE Paper No. 18836) found that critical water fraction when inversion occurred was dramatically reduced with the increment of oil viscosity, and the existing phase inversion models are invalidated. In this paper, an experimental study has been made of high viscosity mineral oil-water flow through a horizontal pipe loop. Results indicate that phase inversion for oil phase with high viscosity occurs much earlier than low viscosity oil, and phase inversion tends to be delayed, with the increment in experimental temperature. The influence of mixture velocities on the inversion process could be neglected in the range of mixture velocities that we studied. As well, inversion point obtain by our experiment are best predicted by the correlation of (1989, “An Analysis of Oil/Water Flow Phenomena in Horizontal Pipes,” SPE Professional Product Operating Symposium , Oklahoma, SPE Paper No. 18836). Models of and (1997, “Phase Inversion Prediction Study,” Rev. Inst. Fr. Pet., 52, pp. 415–424) and and (2002, “Modeling of Phase Inversion Phenomenon in Two-Phase Pipe Flows,” Int. J. Multiph. Flow, 28, pp. 1177–1204), based on minimization of system total energy, seem to be invalidated for high viscosity oil.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleExperiment Research of Phase Inversion in Mineral Oil-Water Two-Phase Flow in Horizontal Pipe
    typeJournal Paper
    journal volume131
    journal issue4
    journal titleJournal of Energy Resources Technology
    identifier doi10.1115/1.4000324
    journal fristpage43001
    identifier eissn1528-8994
    keywordsPipes
    keywordsWater
    keywordsFlow (Dynamics)
    keywordsViscosity
    keywordsMixtures
    keywordsPressure drop AND Two-phase flow
    treeJournal of Energy Resources Technology:;2009:;volume( 131 ):;issue: 004
    contenttypeFulltext
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