2018
DOI: 10.1061/(asce)hy.1943-7900.0001490
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Developments and Limits of Discrete Vapor Cavity Models of Transient Cavitating Pipe Flow: 1D and 2D Flow Numerical Analysis

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Cited by 16 publications
(11 citation statements)
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“…For cases of V 0 ¼ 0.71 m/s and V 0 ¼ 1.40 m/s, the DVCM and DGCM perform poorly in predicting the formation and collapse of multiple cavities in the transient process. The classical DVCM is only slightly sensitive to grid number N x (Santoro et al 2018). As shown in Figure 4(d), the vapor fractions of the largest cavity calculated by both models are within the limitation of 10% of each pipe section.…”
Section: Comparison Of Numerical Results For Frictionless Casementioning
confidence: 77%
“…For cases of V 0 ¼ 0.71 m/s and V 0 ¼ 1.40 m/s, the DVCM and DGCM perform poorly in predicting the formation and collapse of multiple cavities in the transient process. The classical DVCM is only slightly sensitive to grid number N x (Santoro et al 2018). As shown in Figure 4(d), the vapor fractions of the largest cavity calculated by both models are within the limitation of 10% of each pipe section.…”
Section: Comparison Of Numerical Results For Frictionless Casementioning
confidence: 77%
“…The first mathematical models of vapor cavity formation and collapse were based on the graphical method [60]. Subsequently, a variety of numerical models (e.g., the discrete vapor cavity model (DVCM) [61][62][63][64], the discrete gas cavity model (DGCM) [65][66][67], the generalized interface vapor cavity model (GIVCM)) [68] were developed leading to a better understanding of the water hammer phenomenon with column separation [69][70][71]. The numerical results were compared against experimental data to assess the limitation of the numerical models [72,73].…”
Section: Present Day: Current Researchmentioning
confidence: 99%
“…Then the head pressure and tail pressure of the pig are brought into the pig model to calculate the speed of the pig. 4) Discrete Vapour Cavity Model (DVCM) Establishing a discrete vapor cavity model is to determine whether liquid column separation will occur in the pipeline [40]- [46]. As shown in Figure 6, we make the following assumptions: When the steam chamber is concentrated at section i, the incoming flow is Q i,in and the outgoing flow is Q i,out .…”
Section: A Mathematical Modelmentioning
confidence: 99%