2018
DOI: 10.1016/j.ijheatfluidflow.2018.04.016
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Flow characteristics in a volute-type centrifugal pump using large eddy simulation

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Cited by 74 publications
(24 citation statements)
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“…(node,t) = P(node)+P(node,t) (11) where the numerical value of P(node) is defined the arithmetic mean value of pressure in one revolution (12) where N is the number of time steps, t0 is the initial moment and ∆ is the time step length. Thus the value of P(node,t) is the difference between instantaneous pressure value (node,t) and P(node) P(node,t)=P(node,t)-P(node) (13) ̃( , ) is worth in-depth study as it indicates the instability of the inner flow of centrifugal pump. Hence, the dimensionless quantity namely the pressure fluctuation intensity coefficient C P ' is defined as the root-mean-square of P(node,t) divided by reference pressure Pref C P ' = P rms (node) P ref (14) where P rms (node) and Pref are shown in Equations (15) and (16), respectively.…”
Section: Pressure Pulsation Characteristicsmentioning
confidence: 99%
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“…(node,t) = P(node)+P(node,t) (11) where the numerical value of P(node) is defined the arithmetic mean value of pressure in one revolution (12) where N is the number of time steps, t0 is the initial moment and ∆ is the time step length. Thus the value of P(node,t) is the difference between instantaneous pressure value (node,t) and P(node) P(node,t)=P(node,t)-P(node) (13) ̃( , ) is worth in-depth study as it indicates the instability of the inner flow of centrifugal pump. Hence, the dimensionless quantity namely the pressure fluctuation intensity coefficient C P ' is defined as the root-mean-square of P(node,t) divided by reference pressure Pref C P ' = P rms (node) P ref (14) where P rms (node) and Pref are shown in Equations (15) and (16), respectively.…”
Section: Pressure Pulsation Characteristicsmentioning
confidence: 99%
“…In addition, there are also other obvious frequency components rather than f BPF or multiple f n , which are stimulated by a serious complex unsteady flow behaviors, such as the jet-wake pattern along the blade extension direction, the flow impact on the tongue, and the flow separation on the blade suction surface [10][11][12]. The above behaviors usually become more evident under off-design conditions and would take much greater risks for the operation of centrifugal pump [13,14].…”
Section: Introductionmentioning
confidence: 99%
“…In order to explain the pressure fluctuation process under such a working condition, accurate data of the centrifugal pump impeller are required. Compared with the data obtained by ex-perimental measurements [28] and Reynolds-averaged Navier-Stokes (RANS) [29][30][31][32], large eddy simulation (LES) can solve the model with more accurate data of internal flow and has been applied to the centrifugal pump impeller [33][34][35].…”
Section: Introductionmentioning
confidence: 99%
“…Based on the published works, unsteady pressure pulsation energy within the centrifugal pump is affected by two factors, and one is the fluid distribution characteristics at the BTE and the other is the corresponding intense interacting effect with the tongue. So, if we can control and reduce the striking effect between the fluid discharged from the BTE and the volute tongue, then pressure pulsation energy could be decreased [19][20][21]. For the commonly used impeller, when the wrap angles from the shroud to the hub streamlines are identical, fluid discharged from the impeller will hit and interact with the tongue simultaneously [22,23], namely with the same phase.…”
Section: Introductionmentioning
confidence: 99%