CLC number: TK124
On-line Access: 2024-08-27
Received: 2023-10-17
Revision Accepted: 2024-05-08
Crosschecked: 2018-01-16
Cited: 0
Clicked: 17098
Jing-zhi Zhang, Jin-pin Lin, Dan Huang, Wei Li. Numerical study of heat transfer characteristics of downward supercritical kerosene flow inside circular tubes[J]. Journal of Zhejiang University Science A, 2018, 19(2): 158-170.
@article{title="Numerical study of heat transfer characteristics of downward supercritical kerosene flow inside circular tubes",
author="Jing-zhi Zhang, Jin-pin Lin, Dan Huang, Wei Li",
journal="Journal of Zhejiang University Science A",
volume="19",
number="2",
pages="158-170",
year="2018",
publisher="Zhejiang University Press & Springer",
doi="10.1631/jzus.A1600276"
}
%0 Journal Article
%T Numerical study of heat transfer characteristics of downward supercritical kerosene flow inside circular tubes
%A Jing-zhi Zhang
%A Jin-pin Lin
%A Dan Huang
%A Wei Li
%J Journal of Zhejiang University SCIENCE A
%V 19
%N 2
%P 158-170
%@ 1673-565X
%D 2018
%I Zhejiang University Press & Springer
%DOI 10.1631/jzus.A1600276
TY - JOUR
T1 - Numerical study of heat transfer characteristics of downward supercritical kerosene flow inside circular tubes
A1 - Jing-zhi Zhang
A1 - Jin-pin Lin
A1 - Dan Huang
A1 - Wei Li
J0 - Journal of Zhejiang University Science A
VL - 19
IS - 2
SP - 158
EP - 170
%@ 1673-565X
Y1 - 2018
PB - Zhejiang University Press & Springer
ER -
DOI - 10.1631/jzus.A1600276
Abstract: The heat transfer characteristics of China RP-3 aviation kerosene flowing in a vertical downward tube with an inner diameter of 4 mm under supercritical pressures are numerically studied. A ten-species surrogate model is used to calculate the thermophysical properties of kerosene and the re-normalization group (RNG) k-ε turbulent model with the enhanced wall treatment is adopted to consider the turbulent effect. The effects of mass flow rate, wall heat flux, inlet temperature, and pressure on heat transfer are investigated. The numerical results show that three types of heat transfer deterioration exist for the aviation kerosene flow. The first type of deterioration occurred at the tube inlet region and is caused by the development of the thermal boundary layer, while the other two types are observed when the inner wall temperature or the bulk fuel temperature approaches the pseudo-critical temperature. The heat transfer coefficient increases with the increasing mass flow rate and the decreasing wall heat flux, while the inlet bulk fluid temperature only influences the starting point of the heat transfer coefficient curve plotted against the bulk fluid temperature. The increase of inlet pressure can effectively eliminate the deterioration due to the small variations of properties near the pseudo-critical point at relatively high pressure. The numerical heat transfer coefficients fit well with the empirical correlations, especially at higher pressures (about 5 MPa).
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