2017
DOI: 10.1080/19942060.2016.1267043
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Numerical analysis of non-equilibrium steam condensing flows in various Laval nozzles and cascades

Abstract: When steam is used in fluid machinery, phase transition can occur that affects not only the flow fields but also machine performance. Therefore, to achieve an accurate prediction of steam condensing flow using computational fluid dynamics (CFD), phase-transition phenomena should be considered and a non-equilibrium wet-steam model is required. Such a model is implemented in this study using the in-house code T-Flow, and the flow fields -including phase-transition phenomena -in various Laval nozzles are examined… Show more

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Cited by 10 publications
(6 citation statements)
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“…Nucleation is a significant phenomenon of generating droplets in steam flow and it has a close relationship with supercooling level. Supercooling level is defined by the difference between saturation temperature and vapor temperature (Ts-Tc) and reaches to almost 30~40 Kelvin in most cases of non-equilibrium steam condensing flow [13,14]. Since similar distributions of supercooling level were observed throughout the span locations at constant rotor position, just the distributions near casing region were depicted in Fig.…”
Section: Numerical Resultsmentioning
confidence: 92%
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“…Nucleation is a significant phenomenon of generating droplets in steam flow and it has a close relationship with supercooling level. Supercooling level is defined by the difference between saturation temperature and vapor temperature (Ts-Tc) and reaches to almost 30~40 Kelvin in most cases of non-equilibrium steam condensing flow [13,14]. Since similar distributions of supercooling level were observed throughout the span locations at constant rotor position, just the distributions near casing region were depicted in Fig.…”
Section: Numerical Resultsmentioning
confidence: 92%
“…(2) and 3, the source terms of each phase can be defined and two sets of governing equations are required for vapor and liquid phases in principle (inhomogeneous approach) [22]. However, since the main solver T-Flow is a density based solver which is used to calculate single-phase flow, two-phase flow can be modelled by assuming that the vapor and liquid are well mixed in a single mixture (homogeneous approach) [13][14][15]. The net amounts (vapor + liquid) of inter-phase transfer rates of mass and momentum are assumed to be zero owing to no external gain or loss.…”
Section: Wet-steam Modelmentioning
confidence: 99%
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“…It should be noted that meshing the leading and trailing edges of airfoils is a challenging task in CFD problems. There may be some extra mesh refinements in the leading/trailing edge (see, e.g., [80,81]) or some trim/extension in the geometry of the airfoil (see, e.g., [40,82]) in order to deal with the issue of meshing those regions. In this paper, we used a practical way of geometry extension (see Fig.…”
Section: Validationmentioning
confidence: 99%