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    Low Flow Coefficient Centrifugal Compressor Design for Supercritical CO2

    Source: Journal of Turbomachinery:;2014:;volume( 136 ):;issue: 008::page 81008
    Author:
    Lettieri, C.
    ,
    Baltadjiev, N.
    ,
    Casey, M.
    ,
    Spakovszky, Z.
    DOI: 10.1115/1.4026322
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: This paper presents a design strategy for very low flow coefficient multistage compressors operating with supercritical CO2 for carbon capture and sequestration (CCS) and enhanced oil recovery (EOR). At flow coefficients less than 0.01, the stage efficiency is much reduced due to dissipation in the gaspath and more prominent leakage and windage losses. Instead of using a vaneless diffuser as is standard design practice in such applications, the current design employs a vaned diffuser to decrease the meridional velocity and to widen the gas path. The aim is to achieve a step change in performance. The impeller exit width is increased in a systematic parameter study to explore the limitations of this design strategy and to define the upper limit in efficiency gain. The design strategy is applied to a fullscale reinjection compressor currently in service. Threedimensional, steady, supercritical CO2 computational fluid dynamics (CFD) simulations of the full stage with leakage flows are carried out with the National Institute of Standards and Technology (NIST) real gas model. The design study suggests that a nondimensional impeller exit width parameter b2* = (b2/R)د• of six yields a 3.5 point increase in adiabatic efficiency relative to that of a conventional compressor design with vaneless diffuser. Furthermore, it is shown that in such stages the vaned diffuser limits the overall stability and that the onset of rotating stall is likely caused by vortex shedding near the diffuser leading edge. The inverse of the nondimensional impeller exit width parameter b2* can be interpreted as the Rossby number. The investigation shows that, for very low flow coefficient designs, the Coriolis accelerations dominate the relative flow accelerations, which leads to inverted swirl angle distributions at impeller exit. Combined with the twoordersofmagnitude higher Reynolds number for supercritical CO2, the leading edge vortex shedding occurs at lower flow coefficients than in air suggesting an improved stall margin.
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      Low Flow Coefficient Centrifugal Compressor Design for Supercritical CO2

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    http://yetl.yabesh.ir/yetl1/handle/yetl/156651
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    contributor authorLettieri, C.
    contributor authorBaltadjiev, N.
    contributor authorCasey, M.
    contributor authorSpakovszky, Z.
    date accessioned2017-05-09T01:13:46Z
    date available2017-05-09T01:13:46Z
    date issued2014
    identifier issn0889-504X
    identifier otherturbo_136_08_081008.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/156651
    description abstractThis paper presents a design strategy for very low flow coefficient multistage compressors operating with supercritical CO2 for carbon capture and sequestration (CCS) and enhanced oil recovery (EOR). At flow coefficients less than 0.01, the stage efficiency is much reduced due to dissipation in the gaspath and more prominent leakage and windage losses. Instead of using a vaneless diffuser as is standard design practice in such applications, the current design employs a vaned diffuser to decrease the meridional velocity and to widen the gas path. The aim is to achieve a step change in performance. The impeller exit width is increased in a systematic parameter study to explore the limitations of this design strategy and to define the upper limit in efficiency gain. The design strategy is applied to a fullscale reinjection compressor currently in service. Threedimensional, steady, supercritical CO2 computational fluid dynamics (CFD) simulations of the full stage with leakage flows are carried out with the National Institute of Standards and Technology (NIST) real gas model. The design study suggests that a nondimensional impeller exit width parameter b2* = (b2/R)د• of six yields a 3.5 point increase in adiabatic efficiency relative to that of a conventional compressor design with vaneless diffuser. Furthermore, it is shown that in such stages the vaned diffuser limits the overall stability and that the onset of rotating stall is likely caused by vortex shedding near the diffuser leading edge. The inverse of the nondimensional impeller exit width parameter b2* can be interpreted as the Rossby number. The investigation shows that, for very low flow coefficient designs, the Coriolis accelerations dominate the relative flow accelerations, which leads to inverted swirl angle distributions at impeller exit. Combined with the twoordersofmagnitude higher Reynolds number for supercritical CO2, the leading edge vortex shedding occurs at lower flow coefficients than in air suggesting an improved stall margin.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleLow Flow Coefficient Centrifugal Compressor Design for Supercritical CO2
    typeJournal Paper
    journal volume136
    journal issue8
    journal titleJournal of Turbomachinery
    identifier doi10.1115/1.4026322
    journal fristpage81008
    journal lastpage81008
    identifier eissn1528-8900
    treeJournal of Turbomachinery:;2014:;volume( 136 ):;issue: 008
    contenttypeFulltext
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