TY  - CONF
KW  - Drops; Heat transfer coefficients; Heat transfer performance; Mass transfer; Thermal Engineering; Turbulence models
KW  -  Boiling flows; Boiling heat transfer; Engineering fields; Heat transfer performance; Heat transfer process; Mass-flow rate; Numerical investigations; Oval tube; Thermal engineering; Transfer rates
KW  -  Heat flux
SP  - 1919
ID  - scholars17648
TI  - Numerical Investigation of Boiling Flow in Oval Tube with Different Ellipticity
N1  - cited By 0; Conference of 1st International Conference on Technologies for Smart Green Connected Society 2021, ICTSGS 2021 ; Conference Date: 29 November 2021 Through 30 November 2021; Conference Code:179026
N2  - Improving heat transfer has been the continuous quest in thermal engineering field. With higher transfer rate required, many researchers have shifted their attention towards boiling heat transfer that offer superior transfer rate. Despite its potential, study on this heat transfer process have not been as extensive as its single-phase counterpart. Particularly, to the best of our knowledge, no study on the boiling heat transfer in oval tube with different ellipticity. Thus, Numerical investigation using RPI wall boiling model and RNG k-ε turbulence model is conducted for different ellipticity of the oval tube. It is found that the heat transfer performance drop as the ellipticity increases with constant perimeter. Decrease of heat flux and increase of mass flow rate have positive impacts toward the heat transfer performance. The vapour generation resulting by the heat flux and mass flow rate is having high influence in the heat transfer coefficient and pressure drop. © The Electrochemical Society
AV  - none
VL  - 107
EP  - 1931
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-85130541011&doi=10.1149%2f10701.1919ecst&partnerID=40&md5=705b9f3689e18cf8b68cd15af07b5cbd
A1  - Liaw, K.L.
A1  - Kurnia, J.C.
SN  - 19386737
PB  - Institute of Physics
Y1  - 2022///
ER  -