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1.上海交通大学 上海 200240
2.中国核动力研究设计院 成都 610213
Received:07 February 2018,
Revised:20 April 2018,
Published:10 July 2018
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Jun YAO, Bin CHEN, Shouhua JIAO, et al. Experimental study on natural convective heat transfer with bottom curved heating surface in a rectangular enclosure[J]. Nuclear techniques, 2018, 41(7): 070601
Jun YAO, Bin CHEN, Shouhua JIAO, et al. Experimental study on natural convective heat transfer with bottom curved heating surface in a rectangular enclosure[J]. Nuclear techniques, 2018, 41(7): 070601 DOI: 10.11889/j.0253-3219.2018.hjs.41.070601.
小型模块化反应堆的安全壳上封头被设计浸没在大量冷却剂中,在严重事故发生后,安全壳内的堆芯余热通过上封头外部的自然对流排出。为了研究安全壳上封头外部自然对流换热的二维特性,利用一个矩形封闭腔装置,在底部弧形面加热及常压条件下,开展了换热实验。同时利用粒子图像测速法(Particle Image Velocimetry,PIV)测量了弧形加热面周围的流场形态。研究发现:平均努塞尔特数(
Nu
)随加热功率而增大,但增长速率呈降低趋势;沿着弧形加热面向上,局部换热强度先减小后增大,在弧形面40°附近达到最低值;PIV测量结果展示了加热面周围流场形态;主流区的流动速度分层现象明显,且在
X
=50 mm前后的分层趋势相反,其主要源于横向速度的差异;最大流速与加热功率无关,功率主要影响主流区域的流动速度和其横向速度分量。
Background
2
In the design of some small modular reactor (SMR)
the upper head of containment vessel is immersed in a large amount of coolant. After a severe accident
the residual heat inside containment vessel is then removed by natural convection above the upper head.
Purpose
2
This study aims to undertake research into the two-dimensional natural convective heat transfer above the upper head of containment vessel and the flow field around it.
Methods
2
A rectangular enclosure device with bottom curved heating surface was utilized to perform experiments under normal pressure. Particle image velocimetry (PIV) technique was employed to measure flow field.
Results
2
The average
Nu
number
local heat transfer intensity
velocity field due to curved heating surface were obtained and analyzed.
Conclusion
2
The average
Nu
number rises as heating power increases
while the growth rate has a descending trend. Along curved heating surface
local heat transfer intensity decreases first and then increases
lowest value of which occurs near 40° position of curved heating surface. Flow field around curved heating surface is visually revealed. Flow stratification becomes obvious near bulk flow
and the trend after
X
=50 mm is reverse. Stratification is mainly due to the horizontal component of velocity. The maximum velocity is irrelevant to heating power
whose major influence lies upon the velocity of bulk flow and its horizontal component.
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