scholarly journals Power transient critical heat flux in a narrow rectangular channel under downward flow

Author(s):  
Huiyung Kim ◽  
Jeongmin Moon ◽  
Taeho Kim ◽  
Jae Jun Jeong ◽  
Byongjo Yun
Author(s):  
Huiyung Kim ◽  
Jinhoon Kang ◽  
Taehwan Ahn ◽  
Jae Jun Jeong ◽  
Byongjo Yun

1995 ◽  
Vol 117 (2) ◽  
pp. 536-538 ◽  
Author(s):  
X. C. Huang ◽  
S. W. Ruan ◽  
G. Bartsch

2002 ◽  
Vol 39 (7) ◽  
pp. 736-742 ◽  
Author(s):  
Futoshi TANAKA ◽  
Kaichiro MISHIMA ◽  
Tamio KOHRIYAMA ◽  
Yukimitsu OKANO

2018 ◽  
Vol 84 (859) ◽  
pp. 17-00380-17-00380
Author(s):  
Yoshiki KAWAZOE ◽  
Takeyuki AMI ◽  
Hisashi UMEKAWA ◽  
Mamoru OZAWA

1964 ◽  
Vol 86 (1) ◽  
pp. 12-22 ◽  
Author(s):  
F. E. Tippets

High-speed motion pictures (4300 pictures/sec) of boiling water flow patterns in conditions of forced flow at 1000 psia pressure in a vertical heated rectangular channel were taken over the range of mass velocities from 50 to 400 lb/sec-ft2, fluid states from bulk subcooled liquid flow to bulk boiling flow at 0.66 steam quality, and heat fluxes up to and including the critical heat flux level. Eighty critical heat flux determinations were made in the course of the experiment at 1000 psia in conditions of bulk boiling. The motion pictures provide photographic evidence of the general arrangement of the flow in conditions of bulk boiling at high pressure with heat fluxes near and including the critical heat flux level.


2014 ◽  
Vol 2014.19 (0) ◽  
pp. 167-170
Author(s):  
Takayuki HARADA ◽  
Syota FUJIYOSHI ◽  
Takeyuki AMI ◽  
Hisashi UMEKAWA ◽  
Mamoru OZAWA ◽  
...  

2015 ◽  
Vol 2015 (0) ◽  
pp. _B143-1_-_B143-2_
Author(s):  
Takayuki HARADA ◽  
Takeyuki AMI ◽  
Hisashi UMEKAWA ◽  
Mamoru OZAWA

1999 ◽  
Vol 121 (2) ◽  
pp. 394-404 ◽  
Author(s):  
J. C. Sturgis ◽  
I. Mudawar

An experimental study was undertaken to examine the enhancement in critical heat flux (CHF) provided by streamwise curvature. Curved and straight rectangular flow channels were fabricated with identical 5.0 × 2.5 mm cross sections and heated lengths of 101.6 mm in which the heat was applied to only one wall—the concave wall (32.3 mm radius) in the curved channel and a side wall in the straight. Tests were conducted using FC-72 liquid with mean inlet velocity and outlet subcooling of 0.25 to 10 m s−1 and 3 to 29°C, respectively. Centripetal acceleration for curved flow reached 315 times earth’s gravitational acceleration. Critical heat flux was enhanced due to flow curvature at all conditions but the enhancement decreased with increasing subcooling. For near-saturated conditions, the enhancement was approximately 60 percent while for highly subcooled flow it was only 20 percent. The causes for the enhancement were identified as (1) increased pressure on the liquid-vapor interface at wetting fronts, (2) buoyancy forces and (3) increased subcooling at the concave wall. Flow visualization tests were conducted in transparent channels to explore the role of buoyancy forces in enhancing the critical heat flux. These forces were observed to remove vapor from the concave wall and distribute it throughout the cross section. Vapor removal was only effective at near-saturated conditions, yielding the observed substantial enhancement in CHF relative to the straight channel.


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