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Experimental Heat Transfer
A Journal of Thermal Energy Generation, Transport, Storage, and Conversion
Volume 32, 2019 - Issue 1
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Articles

Numerical and experimental analysis of a heat-pipe-embedded printed circuit board for solid state lighting applications

, , , &
Pages 1-13 | Received 05 Jul 2017, Accepted 24 Oct 2017, Published online: 27 Nov 2017
 

ABSTRACT

Thermal management is one of the main issues for electronics cooling especially for tightly packaged PCBs that experience local heat generation. Thus, theoretical and experimental investigations have been conducted to predict thermal performance of a novel heat-pipe-embedded-PCB. First, plain heat-pipe is experimentally tested under various inclination angles and validated by theoretical and numerical calculations. Flattened heat-pipes have been embedded into PCB prototypes made of polymer and aluminum and have been tested for similar experimental parameters; they have shown a decrease in Rtotal compared with conventional heat pipe. Accordingly, reduction of Rtotal  approximately 50% is achieved for both embedded PCB prototypes.

Acknowledgements

The funding for this project was provided by the Turkish Ministry of Science and Technology under the grant number 01464.STZ.2012-2. This work was supported by the Istanbul Development Agency under the contract number ISTKABIL26 and ISTKATR10/15/YNK/0029. The authors would like to thank FARBA Corporation for their support in building the experimental setup.

Nomenclature

A=

surface area, (m2)

d=

diameter, (m)

g=

gravity, (m/s2)

h=

heat transfer cofficient, (W/m2 ·K)

hfg=

enthalpy of vaporization, (J/kg)

K=

permeability

L=

length, (m)

m˙=

mass flow rate, (kg/s)

P=

pressure, (Pa)

q=

total heat transport, (W)

Q˙=

energy, (J/s)

r=

radius, (m)

R=

thermal resistance, (oC/W)

rn=

radius of the nucleation

T=

temperature, (oC)

Dimensionless groups

f=

friction factor

Nu=

Nusselt number

Pr=

Prandtl number

Ra=

Rayleigh number

Greek Symbols

Δp=

Pressure difference, (Pa)

α=

diffusivity, (m2/s)

ε=

emissivity of the surface

=

infinite

K=

thermal conductivity, (W/m·K)

μ=

Dynamic viscosity, (kg/m·s)

ν=

kinematic viscosity, (m2/s)

ψ=

Axial angle

θ=

surface angle, (rad)

ρ=

density, (kg/m3)

σ=

surface tension, (N/m)

Subscripts

a=

adiabatic

b=

boiling

cap=

capillary

c=

condenser

conv=

convection

eff=

effective

e=

evaporator

en=

entrainment

EES=

engineering equation solver

h=

hydrostatic

HP=

heat pipe

i=

inner

l=

liquid

v=

vapour

rad=

radiation

So=

sonic

Surr=

surrounding

O=

outside

PSB=

printed circuit board

wi=

wick

Additional information

Funding

This work was supported by the Turkish Ministry of Science and Technology; [01464.STZ.2012-2]; Istanbul Development Agency; [ISTKABIL26]; [ISTKATR10/15/YNK/0029].

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