VGB POWERTECH 11 (2019)
VGB PowerTech - International Journal for Generation and Storage of Electricity and Heat. Issue 11 (2019). Technical Journal of the VGB PowerTech Association. Energy is us! Power plant operation: legal & technology. Pumped hydro storage. Latent heat storages.
VGB PowerTech - International Journal for Generation and Storage of Electricity and Heat. Issue 11 (2019).
Technical Journal of the VGB PowerTech Association. Energy is us!
Power plant operation: legal & technology. Pumped hydro storage. Latent heat storages.
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Sub-cooled boiling of natural circulation in narrow rectangular channels <strong>VGB</strong> PowerTech <strong>11</strong> l <strong>2019</strong><br />
Calculation results kW/m 2 K<br />
6<br />
5<br />
4<br />
3<br />
2<br />
1<br />
+30 %<br />
Cao correlation<br />
Hong correlation<br />
Rohsenow correlation<br />
-30 %<br />
ature, as well as the size of narrow rectangular<br />
channels.<br />
––<br />
For natural circulation systems, the generation<br />
and detachment of bubbles have<br />
an influence on heat transfer coefficient<br />
during sub-cooled boiling. This<br />
process is accompanied by flow oscillation.<br />
It is discovered that there are 3<br />
stages during the sub-cooled boiling<br />
phenomenon.<br />
––<br />
The empirical correlation has been proposed<br />
for the heat transfer coefficient of<br />
sub-cooled boiling, during natural circulation<br />
through narrow rectangular channels.<br />
It has been derived using dimensionless<br />
analysis method. All experiment<br />
results fall within ±15 % of the proposed<br />
correlation.<br />
apart from just the heat flux. In addition, as<br />
seen from F i g u r e 7, the generation and<br />
disappearance of bubbles which has a great<br />
influence on the volume flow rate leads to<br />
a instability in the process of sub-cooled<br />
boiling. This decreases the heat transfer coefficient.<br />
Although Cao and Hong correlations<br />
fit well with the experiment results,<br />
they can’t reflect the process of sub-cooled<br />
boiling. In this paper, dimensional analysis<br />
method has been performed in order to realize<br />
an empirical correlation for the heat<br />
transfer coefficient of sub-cooled boiling in<br />
natural circulation.<br />
According to the results of previous studies<br />
[10, 21, 25] and experiment results based<br />
on F i g u r e 1 , the governing factors which<br />
influence the heat transfer coefficient for<br />
natural circulation sub-cooled boiling phenomenon<br />
have been identified. Ta b l e 3<br />
gives a comprehensive list of such factors.<br />
According to the π theorem [26], D e , , f ,<br />
are selected as the fundamental variables<br />
to be analyzed and the equation (7) describing<br />
the heat transfer coefficient of subcooled<br />
boiling in natural circulation can be<br />
obtained.<br />
(7)<br />
The equation (7) is fitted based on the experiment<br />
results of the natural circulation<br />
system. The resulting empirical correlation<br />
is shown as Equation (8)-(9).<br />
(8)<br />
<br />
0<br />
0 1 2 3 4 5 6<br />
Experiment results kW/m 2 K<br />
Fig. 9. Comparison between calculation and experiment results.<br />
(9)<br />
F i g u r e 10 shows the calculation results<br />
using above correlation, as compared with<br />
Tab. 3. Dimensional parameters.<br />
the experiment results for the natural circulation<br />
system.<br />
As depicted in F i g u r e 10 , the calculation<br />
results show a good fit with the experiment<br />
results within an accuracy of ±15 %. In<br />
contrast to the previous studies, dimensional<br />
analysis method has been used to<br />
formulate the empirical correlation, which<br />
can describe the physical process about<br />
sub-cooled boiling of natural circulation in<br />
narrow rectangular channels.<br />
Conclusions<br />
Based on the experiments of sub-cooled<br />
boiling in natural circulation, different factors<br />
have been identified and investigated,<br />
which have an effect on heat transfer coefficient.<br />
The following conclusions have<br />
been drawn from this study:<br />
––<br />
For sub-cooled boiling, the heat transfer<br />
coefficient increases with an increase in<br />
the heating power and decreases with an<br />
increase in the inlet sub-cooling temper-<br />
Acknowledgments<br />
The research was funded by National Natural<br />
Science Foundation of China<br />
(No.50976033), Beijing Natural Science<br />
Foundation (No.3172032) and<br />
Nomenclature Meaning of nomenclature Unit Dimension<br />
h Heat transfer coefficient kW(/m 2 K) MT –3 –1<br />
D e Hydraulic diameter of heating channel m L<br />
Liquid thermal conductivity kW/(m K) MLT –3 –1<br />
V Thermal expansion coefficient K - 1 –1<br />
g Gravitational acceleration m/s 2 LT –2<br />
∆T Sub-cooling degree K <br />
q Heat flux kW/m 2 MT –3<br />
C p Constant specific heat capacity kJ/(kg K) L 2 T –2 –1<br />
Fluid density Kg/m 3 ML –3<br />
f Dynamic viscosity of fluid Pa˙s ML –1 T –1<br />
w Dynamic viscosity of fluid near wall Pa˙s ML –1 T –1<br />
Length-width ratio of experiment cross-section Dimensionless N/A<br />
Fundamental Research Funds for Central<br />
Universities (No.2017XS086). Finally, the<br />
authors would also like to thank the<br />
researchers of Institute of Nuclear Thermal<br />
Safety and Standardization for their<br />
contribution.<br />
References<br />
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[2] Ishibashi, Nishikawak. Saturated boiling<br />
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863-866.<br />
[3] Sun L, Mishima K. An evaluation of prediction<br />
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