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- W1990493769 abstract "An experimental study was carried out to understand the phenomena of the boiling flow of liquid nitrogen in an inclined tube with closed bottom by using a high speed motion analyzer. The experimental tube is 0.018 mID and 1.0 m in length. The range of the inclination angle is 45°–90° from the horizontal. The experiment focusedon the effect of the inclination angle show that the mean liquid slug length and Taylor bubble length increase withthe increasing x/D at various inclination angles. At the same x/D, the mean liquid slug length and Taylor bubble length increase first, and then decrease with decreasing inclination angles, with the maximum at 60°. In the verticaltube, standard deviation of the nitrogen Taylor bubble length increase with the increasing x/D. For the inclined tube, standard deviation of the nitrogen Taylor bubble length increases first, and then decreases with the increasing x/D. Standard deviation of the liquid slug length increases with increasing x/D for all inclination angles." @default.
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- W1990493769 date "2009-02-01" @default.
- W1990493769 modified "2023-09-24" @default.
- W1990493769 title "Cryogenic Liquid Slug and Taylor Bubble Length Distributions in an Inclined Tube" @default.
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- W1990493769 doi "https://doi.org/10.1016/s1004-9541(09)60027-6" @default.
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