Low Flow Coefficient Centrifugal Compressor Design for Supercritical CO2Source: Journal of Turbomachinery:;2014:;volume( 136 ):;issue: 008::page 81008DOI: 10.1115/1.4026322Publisher: 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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| contributor author | Lettieri, C. | |
| contributor author | Baltadjiev, N. | |
| contributor author | Casey, M. | |
| contributor author | Spakovszky, Z. | |
| date accessioned | 2017-05-09T01:13:46Z | |
| date available | 2017-05-09T01:13:46Z | |
| date issued | 2014 | |
| identifier issn | 0889-504X | |
| identifier other | turbo_136_08_081008.pdf | |
| identifier uri | http://yetl.yabesh.ir/yetl/handle/yetl/156651 | |
| description 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. | |
| publisher | The American Society of Mechanical Engineers (ASME) | |
| title | Low Flow Coefficient Centrifugal Compressor Design for Supercritical CO2 | |
| type | Journal Paper | |
| journal volume | 136 | |
| journal issue | 8 | |
| journal title | Journal of Turbomachinery | |
| identifier doi | 10.1115/1.4026322 | |
| journal fristpage | 81008 | |
| journal lastpage | 81008 | |
| identifier eissn | 1528-8900 | |
| tree | Journal of Turbomachinery:;2014:;volume( 136 ):;issue: 008 | |
| contenttype | Fulltext |