Thermocapillary on film boiling heat transfer from a non isothermal horizontal surface: A theoretical study from CANDU reactors

被引:1
作者
Arias, F. J. [1 ]
Pla, P. [2 ]
Reventos, F. [1 ]
机构
[1] Tech Univ Catalonia UPC, Dept Phys & Nucl Engn, Barcelona 08028, Catalonia, Spain
[2] Univ Pisa, Dept Mech Nucl & Prod Engn, San Piero A Grado Nucl Res Grp, I-56100 Pisa, Italy
关键词
CANDU nuclear reactors; Film boiling; Surface tension temperature coefficient; Void coefficient of reactivity;
D O I
10.1016/j.pnucene.2009.02.005
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
Film boiling heat transfer from a horizontal non-isothermal surface is formulated with due consideration to thermocapillary and thermal expansion where thermocapillary convection has been largely ignored in film boiling. The study is particularity important in nuclear reactor technology where non-isothermal heater is practically the general situation due to unavoidable non-axisymmetric neutronic flux in the fuel geometries (cylindrical geometries). Utilizing a simplified geometrical model, an analytical expression was derived. The above equation applied in a sigmoidal temperature profile results in a central stratification for film boiling along the heater's length. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:672 / 675
页数:4
相关论文
共 8 条
[1]  
BENTZ J, 1997, THESIS TECHNICAL U M
[2]  
Berenson PJ., 1961, J HEAT TRANSFER, V83, P351, DOI [DOI 10.1115/1.3682280, 10.1115/1.3682280]
[3]  
BROMLEY LA, 1948, THESIS U CALIFORNIA
[4]  
LANDAU LD, 1991, MECANICA FLUIDOS, V6
[5]  
MAREK A, 1996, THESIS TECHNICAL U M
[6]   The origin of thermocapillary convection in subcooled nucleate pool boiling [J].
Marek, R ;
Straub, J .
INTERNATIONAL JOURNAL OF HEAT AND MASS TRANSFER, 2001, 44 (03) :619-632
[7]  
ROBIN TT, 1970, INT J HEAT MASS TRAN, V13, P305
[8]  
SYNDER NW, 1968, 68HT51 ASME