TY - GEN
T1 - Experiment on evaporation heat transfer performance of porous surface
AU - Hirasawa, Shigeki
AU - Nakajima, Takuya
AU - Urimoto, Tetsuya
AU - Tsujimoto, Yuya
AU - Takeuchi, Yusuke
AU - Kawanami, Tsuyoshi
AU - Shirai, Katsuaki
PY - 2016/7/20
Y1 - 2016/7/20
N2 - Enhancement of evaporation heat transfer performance is important for cooling of electronic devices. Evaporation heat transfer coefficient of two types of porous surfaces supplied with water liquid film was studied experimentally. First porous surface was multi layers of meshed plates with micro-channel of 0.3 mm width. Thin water liquid film was supplied to the porous surface by bubbles. Evaporation heat transfer coefficient of the porous surface with one or two layers of meshed plates was 8×104 W/m2K and it was higher than pool boiling heat transfer coefficient. Second porous surface was 1 mm thickness of glass-beads of 0.4 mm in diameter on a heated cupper plate. Water was supplied to the porous layer at the center of the plate. Evaporation heat transfer coefficient was 1000 W/m2K after water was supplied. Evaporation heat transfer coefficient increased to 7000 W/m2K before appearance of dry portion on the plate, because water film thickness in the porous layer was thin.
AB - Enhancement of evaporation heat transfer performance is important for cooling of electronic devices. Evaporation heat transfer coefficient of two types of porous surfaces supplied with water liquid film was studied experimentally. First porous surface was multi layers of meshed plates with micro-channel of 0.3 mm width. Thin water liquid film was supplied to the porous surface by bubbles. Evaporation heat transfer coefficient of the porous surface with one or two layers of meshed plates was 8×104 W/m2K and it was higher than pool boiling heat transfer coefficient. Second porous surface was 1 mm thickness of glass-beads of 0.4 mm in diameter on a heated cupper plate. Water was supplied to the porous layer at the center of the plate. Evaporation heat transfer coefficient was 1000 W/m2K after water was supplied. Evaporation heat transfer coefficient increased to 7000 W/m2K before appearance of dry portion on the plate, because water film thickness in the porous layer was thin.
KW - Cooling electronic devices
KW - cross-grooved surface
KW - dry portion
KW - evaporation
KW - heat transfer coefficient
KW - pool boiling
KW - porous surface
KW - thin glass-beads layer
UR - http://www.scopus.com/inward/record.url?scp=84983268623&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=84983268623&partnerID=8YFLogxK
U2 - 10.1109/ITHERM.2016.7517520
DO - 10.1109/ITHERM.2016.7517520
M3 - Conference contribution
AN - SCOPUS:84983268623
T3 - Proceedings of the 15th InterSociety Conference on Thermal and Thermomechanical Phenomena in Electronic Systems, ITherm 2016
SP - 1
EP - 5
BT - Proceedings of the 15th InterSociety Conference on Thermal and Thermomechanical Phenomena in Electronic Systems, ITherm 2016
PB - Institute of Electrical and Electronics Engineers Inc.
T2 - 15th InterSociety Conference on Thermal and Thermomechanical Phenomena in Electronic Systems, ITherm 2016
Y2 - 31 May 2016 through 3 June 2016
ER -