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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 />

[1] Tong Mingwei, Shi Chengming, Xin Mingdao.<br />

Heat transfer enhancement in a two<br />

phase closed thermosyphon [J]. Journal of<br />

Engineering Thermophysics., 1984, 5(4):<br />

58-60.<br />

[2] Ishibashi, Nishikawak. Saturated boiling<br />

heat transfer in narrow spaces [J]. International<br />

Journal of Heat and Mass Transfer.,1969,12(8):<br />

863-866.<br />

[3] Sun L, Mishima K. An evaluation of prediction<br />

methods for saturated flow boiling heat<br />

transfer in mini-channels [J]. International<br />

Journal of Heat & Mass Transfer, 2009,<br />

52(23-24): 5323-5329.<br />

[4] Schulz T L. Westinghouse AP1000 advanced<br />

passive plant [J]. Nuclear Engineering &<br />

Design, 2006, 236(14): 1547-1557.<br />

68

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