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BULETINUL INSTITUTULUI POLITEHNIC DIN IAŞI

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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)

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