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
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.