Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow

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KLJENAK, Ivo .
Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow. 
Strojniški vestnik - Journal of Mechanical Engineering, [S.l.], v. 47, n.8, p. 455-461, july 2017. 
ISSN 0039-2480.
Available at: <https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/>. Date accessed: 17 sep. 2021. 
doi:http://dx.doi.org/.
Kljenak, I.
(2001).
Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow.
Strojniški vestnik - Journal of Mechanical Engineering, 47(8), 455-461.
doi:http://dx.doi.org/
@article{.,
	author = {Ivo  Kljenak},
	title = {Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow},
	journal = {Strojniški vestnik - Journal of Mechanical Engineering},
	volume = {47},
	number = {8},
	year = {2001},
	keywords = {physical models; numerical models; void fraction; vertical subcooled nucleate boiling flow; },
	abstract = {A three-dimensional bubble-tracking model, which simulates subcooled nucleate boiling in a heated vertical cylindrical tube, is presented. The behavior of the liquid-vapor system results from motion, interaction and heat transfer mechanisms prescribed mostly at the level of individually-tracked vapor bubbles. The model takes into account bubble nucleation and liquid heating caused by wall heat flux, bubble sliding on the tube wall, bubble departure from the tube wall, bubble condensation in the low-temperature tube core region, bubble interaction through wake drift, bubble collisions and coalescence, bubble radial migration towards the tube core region, and turbulent dispersion in the liquid phase. Simulated void fraction and liquid temperature radial profiles on different axial locations of a heated channel are compared with experimental results from other authors.},
	issn = {0039-2480},	pages = {455-461},	doi = {},
	url = {https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/}
}
Kljenak, I.
2001 July 47. Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow. Strojniški vestnik - Journal of Mechanical Engineering. [Online] 47:8
%A Kljenak, Ivo 
%D 2001
%T Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow
%B 2001
%9 physical models; numerical models; void fraction; vertical subcooled nucleate boiling flow; 
%! Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow
%K physical models; numerical models; void fraction; vertical subcooled nucleate boiling flow; 
%X A three-dimensional bubble-tracking model, which simulates subcooled nucleate boiling in a heated vertical cylindrical tube, is presented. The behavior of the liquid-vapor system results from motion, interaction and heat transfer mechanisms prescribed mostly at the level of individually-tracked vapor bubbles. The model takes into account bubble nucleation and liquid heating caused by wall heat flux, bubble sliding on the tube wall, bubble departure from the tube wall, bubble condensation in the low-temperature tube core region, bubble interaction through wake drift, bubble collisions and coalescence, bubble radial migration towards the tube core region, and turbulent dispersion in the liquid phase. Simulated void fraction and liquid temperature radial profiles on different axial locations of a heated channel are compared with experimental results from other authors.
%U https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/
%0 Journal Article
%R 
%& 455
%P 7
%J Strojniški vestnik - Journal of Mechanical Engineering
%V 47
%N 8
%@ 0039-2480
%8 2017-07-07
%7 2017-07-07
Kljenak, Ivo.
"Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow." Strojniški vestnik - Journal of Mechanical Engineering [Online], 47.8 (2001): 455-461. Web.  17 Sep. 2021
TY  - JOUR
AU  - Kljenak, Ivo 
PY  - 2001
TI  - Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow
JF  - Strojniški vestnik - Journal of Mechanical Engineering
DO  - 
KW  - physical models; numerical models; void fraction; vertical subcooled nucleate boiling flow; 
N2  - A three-dimensional bubble-tracking model, which simulates subcooled nucleate boiling in a heated vertical cylindrical tube, is presented. The behavior of the liquid-vapor system results from motion, interaction and heat transfer mechanisms prescribed mostly at the level of individually-tracked vapor bubbles. The model takes into account bubble nucleation and liquid heating caused by wall heat flux, bubble sliding on the tube wall, bubble departure from the tube wall, bubble condensation in the low-temperature tube core region, bubble interaction through wake drift, bubble collisions and coalescence, bubble radial migration towards the tube core region, and turbulent dispersion in the liquid phase. Simulated void fraction and liquid temperature radial profiles on different axial locations of a heated channel are compared with experimental results from other authors.
UR  - https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/
@article{{}{.},
	author = {Kljenak, I.},
	title = {Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow},
	journal = {Strojniški vestnik - Journal of Mechanical Engineering},
	volume = {47},
	number = {8},
	year = {2001},
	doi = {},
	url = {https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/}
}
TY  - JOUR
AU  - Kljenak, Ivo 
PY  - 2017/07/07
TI  - Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow
JF  - Strojniški vestnik - Journal of Mechanical Engineering; Vol 47, No 8 (2001): Strojniški vestnik - Journal of Mechanical Engineering
DO  - 
KW  - physical models, numerical models, void fraction, vertical subcooled nucleate boiling flow, 
N2  - A three-dimensional bubble-tracking model, which simulates subcooled nucleate boiling in a heated vertical cylindrical tube, is presented. The behavior of the liquid-vapor system results from motion, interaction and heat transfer mechanisms prescribed mostly at the level of individually-tracked vapor bubbles. The model takes into account bubble nucleation and liquid heating caused by wall heat flux, bubble sliding on the tube wall, bubble departure from the tube wall, bubble condensation in the low-temperature tube core region, bubble interaction through wake drift, bubble collisions and coalescence, bubble radial migration towards the tube core region, and turbulent dispersion in the liquid phase. Simulated void fraction and liquid temperature radial profiles on different axial locations of a heated channel are compared with experimental results from other authors.
UR  - https://www.sv-jme.eu/article/modeling-of-void-fraction-and-liquid-temperature-profile-evolution-in-vertical-subcooled-nucleate-boiling-flow/
Kljenak, Ivo"Modeling of void fraction and liquid temperature profile evolution in vertical subcooled nucleate boiling flow" Strojniški vestnik - Journal of Mechanical Engineering [Online], Volume 47 Number 8 (07 July 2017)

Authors

Affiliations

  • Institute Jožef Štefan, Ljubljana, Slovenia

Paper's information

Strojniški vestnik - Journal of Mechanical Engineering 47(2001)8, 455-461

A three-dimensional bubble-tracking model, which simulates subcooled nucleate boiling in a heated vertical cylindrical tube, is presented. The behavior of the liquid-vapor system results from motion, interaction and heat transfer mechanisms prescribed mostly at the level of individually-tracked vapor bubbles. The model takes into account bubble nucleation and liquid heating caused by wall heat flux, bubble sliding on the tube wall, bubble departure from the tube wall, bubble condensation in the low-temperature tube core region, bubble interaction through wake drift, bubble collisions and coalescence, bubble radial migration towards the tube core region, and turbulent dispersion in the liquid phase. Simulated void fraction and liquid temperature radial profiles on different axial locations of a heated channel are compared with experimental results from other authors.

physical models; numerical models; void fraction; vertical subcooled nucleate boiling flow;