Online proceedings - EDA Publishing Association
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Online proceedings - EDA Publishing Association
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q h<br />
T h<br />
7-9 October 2009, Leuven, Belgium<br />
Heat Source<br />
Heat<br />
Spreader<br />
TEG<br />
P<br />
N<br />
Heat<br />
Sink<br />
q c<br />
T c<br />
I<br />
Fig. 2. Thermoelectric energy scavenging module.<br />
R L<br />
Fig. 1. Schematic of a thermocouple in generation mode.<br />
This section shows a proposed thermoelectric (TE) energy<br />
scavenging module to recover the wasted energy from PA<br />
transistors. This section also presents a fully-coupled TE model<br />
developed to explore the performance and parametric behaviors<br />
of the energy scavenging module.<br />
A. Energy Scavenging Module<br />
An energy scavenging module contains a Cu heat spreader, a<br />
Bi 2 Te 3 based thermoelectric generator (TEG), and a heat sink<br />
as illustrated in Fig. 2. A Cu heat spreader is used to minimize<br />
the thermal resistance between the transistor and the<br />
thermoelectric generator (TEG). Forced-air convection is<br />
utilized for the reliability of high power PAs, e.g. PAs for<br />
macro-cell base stations. Hence, the module contains a heat<br />
sink that enhances the heat transfer from the TEG to the<br />
ambient.<br />
B. Fully-Coupled TE Model<br />
A fully-coupled TE model was developed to explore the<br />
power generation performance as well as the thermal<br />
performance of the energy scavenging module. The TE model<br />
integrates the TE theory with heat transfer theory by<br />
embedding a power generation cycle in a thermal network; as<br />
per Fig. 3. q tot is the total heat flow from the source (the<br />
transistor), q h is the heat flow to the TEG hot side, h, P L is the<br />
generated power by the TEG, and q c is the heat flow out of the<br />
TEG at the TEG cold side, c. j and a denote the junction and<br />
the ambient. θ jh and θ ca are thermal resistances between j and h<br />
and between c and a. Fig. 3 shows basic physics of the TE<br />
model, i.e., heat flow from the source conducts to the TEG, a<br />
fraction of the heat is converted into the useful power, and the<br />
remainder is dissipated to the ambient.<br />
q h and q c can be expressed by the following equations.<br />
q<br />
( ) /<br />
2 tot<br />
= qh<br />
= NIα Th<br />
+ Th<br />
−Tc<br />
θTEG<br />
− NI R / 2 (1)<br />
q = NIα T + ( T −T<br />
) / θ NI<br />
2 R / 2 (2)<br />
c c h c TEG +<br />
where N is the number of thermocouples, I is the generated<br />
current, α is the Seebeck coefficient, T h and T c are temperatures<br />
of hot and cold sides of the TEG, respectively, θ TEG is the TEG<br />
thermal resistance, R is the electrical resistance of a<br />
thermocouple. Equation (1) shows that q tot is equal to q h . It is<br />
based on the assumption that the heat loss from the source to<br />
the ambient is negligible compared with the heat flow<br />
conducting through the heat spreader to the TEG hot side.<br />
In (1) and (2), the first terms, NIαT h and NIαT c are the energy<br />
terms due to Peltier effect, the 2nd term, (T h -T c )/θ TEG is the heat<br />
conduction purely due to the temperature difference across<br />
pellets, the 3rd term, NI 2 R/2 is the Joule heating effect. The<br />
further information including the derivation of q h and q c in the<br />
form of three terms can be found in the literature [14].<br />
q h and q c can be expressed in the form of heat flows between<br />
j and h and heat flow between c and a as<br />
q<br />
q<br />
h<br />
c<br />
( T j −Th<br />
)/<br />
θ jh<br />
= (3)<br />
( Tc<br />
−Ta<br />
)/<br />
θca<br />
= (4)<br />
where T j is the junction temperature and T a is the ambient<br />
temperature.<br />
I is defined as<br />
( T −T<br />
)<br />
N h c<br />
I = α (5)<br />
NR + R<br />
where the numerator is the generated voltage across the TEG,<br />
the denominator is the total electrical resistance of the<br />
generation system evaluated by adding the net electrical<br />
resistance of the TEG, NR to R L .<br />
R is defined as<br />
p<br />
L<br />
H<br />
R = 2 ρ + Rc<br />
(6)<br />
A<br />
where ρ is the electrical resistivity of the pellet, H is the height<br />
of the pellet, A p is the pellet cross sectional area, R c is the<br />
electrical contact resistance of a thermocouple.<br />
R c is defined as<br />
R<br />
c<br />
Rc−ρ<br />
= 4 (7)<br />
A<br />
where R c-ρ is the electrical contact resistivity of a thermocouple.<br />
θ TEG can be defined as<br />
P<br />
θ H<br />
TEG<br />
= 2 N⋅kA<br />
(8)<br />
where k is the thermal conductivity of the pellet.<br />
The generated power, P L , associated with R L is defined as<br />
2<br />
L<br />
R L<br />
p<br />
P = I<br />
(9)<br />
Considering the energy balance in a TEG, one can see that the<br />
©<strong>EDA</strong> <strong>Publishing</strong>/THERMINIC 2009 76<br />
ISBN: 978-2-35500-010-2