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TTa ( n1)<br />

is also considered as inlet temperature of the lump under inspection. T Tan , air<br />

temperature in this lump, is also considered as inlet temperature of next lump.<br />

However, when reverse flow occurs, air flows from bigger numbered lump toward<br />

smaller numbered lump. The last lump receives air from the mask and the air in lump 1<br />

flows back into the chamber.<br />

3.5.2 Convection at HADT lump inner surface<br />

The HADT internal convection is considered forced convection only because its small<br />

internal dimension does not give much space for natural convection to develop. Nusselt<br />

number for internal forced convection can be expressed as [57]:<br />

Nu 0.052Re Pr f<br />

(3.71)<br />

Ti Ti a T<br />

f T is the Darcy-Weisbach friction factor explained in chapter 2 which gives<br />

0.5625<br />

fT . Thus Nusselt number above becomes:<br />

Re<br />

0.125<br />

Ti<br />

Nu 0.02925Re Pr<br />

(3.72)<br />

0.875 0.5<br />

Ti Ti a<br />

Therefore the convectional resistance on HADT lump inner surface is:<br />

R<br />

Ticn<br />

3.5.3 Convection at HADT lump outer surface<br />

1<br />

(3.73)<br />

0.875 0.5 kma ATli<br />

0.02925ReTi Pra<br />

<br />

The HADT may be modelled as a horizontal cylinder and the natural convectional<br />

thermal resistance at an HADT lump outer surface may be expressed as [55]:<br />

R<br />

Toc<br />

63<br />

Ti<br />

1<br />

(3.74)<br />

kma AToc 0.148<br />

1.02 RaTo<br />

<br />

However, the HADT outer surface is corrugated (Figure 3.15). The corrugation<br />

increases the surface area as well as the convection. A Toc in Eq. (3.74) is the corrugated<br />

To

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