Prediction of the minimum point of the pressure drop in a narrow rectangular channel under a transversely non-uniform heat flux

2018 ◽  
Vol 122 ◽  
pp. 163-174 ◽  
Author(s):  
Taewoo Kim ◽  
Yong Jae Song ◽  
Omar S. Al-Yahia ◽  
Daeseong Jo
1998 ◽  
Vol 120 (4) ◽  
pp. 260-269 ◽  
Author(s):  
S. D. Dahl ◽  
J. H. Davidson

An important issue arising from prior studies of thermosyphon heat exchangers for use in solar water heaters is the need for heat transfer and pressure drop correlations for the laminar, mixed-convection regime in which these many of these heat exchangers operate. In this paper, we present empirical correlations for tube-in-shell heat exchangers with the thermosyphon flow on the shell side. The correlations are determined for uniform heat flux on the tube walls. Ranges of Reynolds and Grashof numbers are 130 to 2,000 and 4 × 105 to 8 × 107, respectively. Nusselt number correlations are presented in a form that combines the contributions of forced and natural convection. Mixed convection dominates forced convection heat transfer in these geometries. Pressure drop is not significantly affected by mixed convection.


1981 ◽  
Vol 103 (4) ◽  
pp. 667-672 ◽  
Author(s):  
K. H. Sun ◽  
R. B. Duffey ◽  
C. Lin

A thermal-hydraulic model has been developed for describing the phenomenon of hydrodynamically-controlled dryout, or the boil-off phenomenon, in a vertical channel with a spatially-averaged or uniform heat flux. The use of the drift flux correlation for the void fraction profile, along with mass and energy balances for the system, leads to a dimensionless closed-form solution for the predictions of two-phase mixture levels and collapsed liquid levels. The physical significance of the governing dimensionless parameters are discussed. Comparisons with data from single-tube experiments, a 3 × 3 rod bundle experiment, and the Three Mile Island nuclear power plant show good agreement.


2011 ◽  
Vol 83 (2) ◽  
Author(s):  
Francisco Vega Reyes ◽  
Vicente Garzó ◽  
Andrés Santos

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