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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

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