Numerical Prediction for Subcooled Boiling Flow of Liquid Nitrogen in a Vertical Tube with MUSIG Model
Multiple size group (MUSIG) model combined with a threedimensional twofluid model were em ployed to predict subcooled boiling flow of liquid nitrogen in a vertical upward tube. Based on the mechanism of boiling heat transfer, some important bubble model parameters were amended to be applicable to th...
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Published in | Chinese journal of chemical engineering Vol. 21; no. 11; pp. 1195 - 1205 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Elsevier B.V
01.11.2013
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Subjects | |
Online Access | Get full text |
ISSN | 1004-9541 2210-321X |
DOI | 10.1016/S1004-9541(13)60632-1 |
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Abstract | Multiple size group (MUSIG) model combined with a threedimensional twofluid model were em ployed to predict subcooled boiling flow of liquid nitrogen in a vertical upward tube. Based on the mechanism of boiling heat transfer, some important bubble model parameters were amended to be applicable to the modeling of liquid nitrogen. The distribution of different discrete bubble classes was demonstrated numerically and the distribu tion patterns of void fraction in the wallheated tube were analyzed. It was found that the average void fraction in creases nonlinearly along the axial direction with wall heat flux and it decreases with inlet mass flow rate and sub cooled temperature. The local void fraction exhibited a Ushape distribution in the radial direction. The partition of the wall heat flux along the tube was obtained. The results showed that heat flux consumed on evaporation is the leading part of surface heat transfer at the rear region of subcooled boiling. The turning point in the pressure drop curve reflects the instability of bubbly flow. Good agreement was achieved on the local heat transfer coefficient aalnst experimental measurements, which demonstrated the accuracy of the numerical model. |
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AbstractList | Multiple size group (MUSIG) model combined with a three-dimensional two-fluid model were employed to predict subcooled boiling flow of liquid nitrogen in a vertical upward tube. Based on the mechanism of boiling heat transfer, some important bubble model parameters were amended to be applicable to the modeling of liquid nitrogen. The distribution of different discrete bubble classes was demonstrated numerically and the distribution patterns of void fraction in the wall-heated tube were analyzed. It was found that the average void fraction increases nonlinearly along the axial direction with wall heat flux and it decreases with inlet mass flow rate and subcooled temperature. The local void fraction exhibited a U-shape distribution in the radial direction. The partition of the wall heat flux along the tube was obtained. The results showed that heat flux consumed on evaporation is the leading part of surface heat transfer at the rear region of subcooled boiling. The turning point in the pressure drop curve reflects the instability of bubbly flow. Good agreement was achieved on the local heat transfer coefficient against experimental measurements, which demonstrated the accuracy of the numerical model. Multiple size group (MUSIG) model combined with a threedimensional twofluid model were em ployed to predict subcooled boiling flow of liquid nitrogen in a vertical upward tube. Based on the mechanism of boiling heat transfer, some important bubble model parameters were amended to be applicable to the modeling of liquid nitrogen. The distribution of different discrete bubble classes was demonstrated numerically and the distribu tion patterns of void fraction in the wallheated tube were analyzed. It was found that the average void fraction in creases nonlinearly along the axial direction with wall heat flux and it decreases with inlet mass flow rate and sub cooled temperature. The local void fraction exhibited a Ushape distribution in the radial direction. The partition of the wall heat flux along the tube was obtained. The results showed that heat flux consumed on evaporation is the leading part of surface heat transfer at the rear region of subcooled boiling. The turning point in the pressure drop curve reflects the instability of bubbly flow. Good agreement was achieved on the local heat transfer coefficient aalnst experimental measurements, which demonstrated the accuracy of the numerical model. |
Author | 王斯民 文键 李亚梅 杨辉著 厉彦忠 JiyuanTu |
AuthorAffiliation | School of Energy and Power Engineering, Xi'an Jiaotong University, Xi'an 710049, China School of Aerospace, Mechanica-1 and Manufacturing, RMIT University, VIC 3083, Australia |
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CitedBy_id | crossref_primary_10_1016_j_cjche_2018_11_028 crossref_primary_10_1016_j_ijmultiphaseflow_2023_104428 crossref_primary_10_1016_j_applthermaleng_2021_117160 crossref_primary_10_1016_j_pnucene_2021_103773 crossref_primary_10_1016_j_ijheatmasstransfer_2017_06_097 |
Cites_doi | 10.1016/0011-2275(83)90092-9 10.1016/j.apm.2006.03.010 10.1016/0011-2275(85)90207-3 10.1016/j.ces.2004.04.023 10.1016/0017-9310(69)90154-9 10.1016/0009-2509(96)88489-2 10.1115/1.3450610 10.1016/S0029-5493(00)00337-X 10.1007/s00231-003-0423-2 10.1002/aic.690361004 10.1016/0017-9310(69)90155-0 10.1016/0017-9310(85)90213-3 10.1016/0011-2275(86)90007-X 10.1016/0301-9322(81)90003-3 10.1115/1.1928916 10.1115/1.3450503 10.1016/S0017-9310(01)00230-7 10.1016/j.applthermaleng.2006.02.011 10.1016/0029-5493(95)01160-9 10.1002/aic.690420505 |
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Keywords | liquid nitrogen MUSIG model subcooled boiling bubble frequency nucleation site density bubble departure diameter |
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Notes | 11-3270/TQ liquid nitrogen, subcooled boiling, bubble departure diameter, bubble frequency, nucleation site den-sity, MUSIG model Multiple size group (MUSIG) model combined with a threedimensional twofluid model were em ployed to predict subcooled boiling flow of liquid nitrogen in a vertical upward tube. Based on the mechanism of boiling heat transfer, some important bubble model parameters were amended to be applicable to the modeling of liquid nitrogen. The distribution of different discrete bubble classes was demonstrated numerically and the distribu tion patterns of void fraction in the wallheated tube were analyzed. It was found that the average void fraction in creases nonlinearly along the axial direction with wall heat flux and it decreases with inlet mass flow rate and sub cooled temperature. The local void fraction exhibited a Ushape distribution in the radial direction. The partition of the wall heat flux along the tube was obtained. The results showed that heat flux consumed on evaporation is the leading part of surface heat transfer at the rear region of subcooled boiling. The turning point in the pressure drop curve reflects the instability of bubbly flow. Good agreement was achieved on the local heat transfer coefficient aalnst experimental measurements, which demonstrated the accuracy of the numerical model. ObjectType-Article-2 SourceType-Scholarly Journals-1 ObjectType-Feature-1 content type line 23 ObjectType-Article-1 ObjectType-Feature-2 |
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Snippet | Multiple size group (MUSIG) model combined with a threedimensional twofluid model were em ployed to predict subcooled boiling flow of liquid nitrogen in a... Multiple size group (MUSIG) model combined with a three-dimensional two-fluid model were employed to predict subcooled boiling flow of liquid nitrogen in a... |
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SubjectTerms | Boiling bubble departure diameter bubble frequency Heat flux Heat transfer Liquid nitrogen Mathematical models MUSIG model nucleation site density subcooled boiling Tubes Void fraction Walls 垂直管 局部传热系数 平均孔隙度 数值预报 模型参数 流动 液态氮 过冷沸腾 |
Title | Numerical Prediction for Subcooled Boiling Flow of Liquid Nitrogen in a Vertical Tube with MUSIG Model |
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