BULETINUL INSTITUTULUI POLITEHNIC DIN IAŞI
buletinul institutului politehnic din iaşi - Universitatea Tehnică ...
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70 Bogdan Horbaniuc et al<br />
Hypotheses:<br />
1. The soil is homogenous and isotropic in terms of thermophysical<br />
properties.<br />
2. The soil is dry (the influence of the humidity is negligible).<br />
3. The soil thermophysical properties are constant.<br />
4. The tube is isothermal longitudinally.<br />
5. The heat propagation is one-dimensional (radial).<br />
In order to get the most general form of the results, dimensionless<br />
temperatures will be used, defined by<br />
t−<br />
t∞<br />
θ =<br />
t − t<br />
HF<br />
∞<br />
.<br />
(1)<br />
The equations that describe the heat transfer phenomenon are:<br />
a) the heat conduction equation in cylindrical coordinates<br />
2<br />
∂θ<br />
⎛<br />
i ∂ θi<br />
1 ∂θ ⎞<br />
= ai<br />
+ i<br />
∂τ 2<br />
;<br />
⎜ ∂ r r ∂r<br />
⎟<br />
(2)<br />
⎝<br />
⎠<br />
where a is the thermal diffusivity and subscript i means W for the wall domain,<br />
respectively S for the soil (SSM) region.<br />
b) the heat balance equation at the wall-SSM interface<br />
λ<br />
W<br />
⎛∂θW<br />
⎞ ⎛∂θ<br />
⎞<br />
⎜<br />
∂r<br />
⎟ ⎜ ⎟<br />
⎝ ⎠ ⎝ ⎠<br />
S<br />
= λS<br />
r= R<br />
∂r<br />
W<br />
r=<br />
RW<br />
, (3)<br />
where λ is the thermal conductivity of the material.<br />
The initial condition is<br />
0<br />
[ ]<br />
τ < 0: θ= θ ∀r∈<br />
R , R . (4)<br />
The boundary conditions are:<br />
i) on the inner tube surface (r = R 0 )<br />
W<br />
= : = = 0. (5)<br />
r R0 θW,0<br />
θ R<br />
ii) at the end of the SSM region (r = R)<br />
⎛∂θS<br />
⎞<br />
r = R: ⎜ = 0, τ<br />
r<br />
⎟<br />
⎝ ⎠<br />
∂<br />
r=<br />
R<br />
≥ 0. (6)