Heat transfer enhancement at solid-liquid and solid-gas interfaces by near-surface coolant agitation

Citation
A. Kruusing et al., Heat transfer enhancement at solid-liquid and solid-gas interfaces by near-surface coolant agitation, IEEE T COMP, 23(3), 2000, pp. 548-554
Citations number
26
Categorie Soggetti
Material Science & Engineering
Journal title
IEEE TRANSACTIONS ON COMPONENTS AND PACKAGING TECHNOLOGIES
ISSN journal
15213331 → ACNP
Volume
23
Issue
3
Year of publication
2000
Pages
548 - 554
Database
ISI
SICI code
1521-3331(200009)23:3<548:HTEASA>2.0.ZU;2-9
Abstract
Heat transfer enhancement from glass ceramic plate to water or air by agita tion of the coolant near the heated surface was investigated. The experimen tal arrangement consisted of a ceramic plate of dimensions of 47 x 35 x 0.2 6 mm(3), attached to a brass vessel with inner dimensions of 34 x 30 x 4 mm (3). The ceramic plate was provided with a 5 x 5 mm(2) size printed heater on the opposite side from the vessel, The temperature held across the plate was recorded by an infra-red camera. The agitation of the coolant in the v essel lair or water) was performed by a vibrating piezoelectric beam of dim ensions of 26.5 x 12 x 0.6 mm(3), fixed at 1 mm distance from the heated pl ate, or alternatively by a magnetic rod of diameter of 2.2 mm and length of 15 mm, The vibration of the beam with amplitude of some tenths of mm peak to peak at frequencies of 200 to 400 Hz caused the sinking of the peak temp erature of the heater from about 90 degrees C to 45 degrees C in case of wa ter as the coolant and from about 110 degrees C to 100 degrees C in the air . The magnetic rod, rotating in water at speed of some rounds per second lo wered the heater's peak temperature from 85 degrees C to 50 to 60 degrees C . The ambient temperature in all experiments was 22 to 25 degrees C and the heating power 1-2 W, The power needed for agitation was about 50 mW in cas e of piezoelectric vibrator and about 1 W in case of the rotating agitator drived by a fan, Using numerical simulation by ANSYS, it was demonstrated, that the temperature distribution across the plate with heater can be satis factorily simulated using a two-dimensional (2-D) model with appropriately enhanced heat conductivity of the plate and heat transfer coefficient from the plate. For the experimental arrangement used the equivalent heat conduc tivity of the ceramic plate in case of agitated liquid fooling was up to 15 0 W/m . K and heat transfer rate up to 300 W/m(2) K.