Heat transfer and flow pattern in co-current downward steam condensation in vertical pipes-I: CFD simulation and experimental measurements

被引:10
作者
Dahikar, Sachin K. [1 ]
Ganguli, Arijit A. [1 ]
Gandhi, Mayurkumar S. [1 ]
Joshi, Jyeshtharaj B. [1 ,2 ]
Vijayan, Pallippattu K. [3 ]
机构
[1] Inst Chem Technol, Dept Chem Engn, Bombay 400019, Maharashtra, India
[2] Homi Bhabha Natl Inst, Bombay 400094, Maharashtra, India
[3] Bhabha Atom Res Ctr, Reactor Engn Div, Bombay 400085, Maharashtra, India
关键词
condensation; phase change; heat transfer; temperature profile; HTC; computational fluid dynamic (CFD); film characteristic; TURBULENT FILM CONDENSATION; BUBBLE-COLUMN REACTORS; GAS-LIQUID FLOW; PLUME DIMENSIONS; HYDRODYNAMICS; MODEL; TUBE;
D O I
10.1002/cjce.21722
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The condensation of pure steam flowing inside a vertical tube has been extensively studied during the last nine decades. Considerable amount of experimental and analytical efforts can be found due to the significance of this subject in practice. In the present work (Part I), experimental investigations have been performed over a range of pressure (0.1<P<0.35MPa) and internal tube diameter (Di=10, 20 and 43mm). A two-dimensional computational fluid dynamic (CFD) simulations have been carried out commercial software Fluent 6.2 [Fluent 6.2, User's Manual to FLUENT 6.2, Fluent Inc., Lebanon, USA, 2005]. CFD results were used to predict the temperature profiles, pressure drop and the heat transfer coefficient, which was in close agreement with the experimental values. The film characteristics predicted by the CFD simulations have been compared qualitatively with the photographic images. Further, the CFD model developed in Part I extended for the analysis of all the experimental data reported in the published literature. (c) 2012 Canadian Society for Chemical Engineering
引用
收藏
页码:959 / 973
页数:15
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