Thermal resistance between cable and duct.
The equation for ducts with bentonite filling is based on the conduction shape factor of a cylinder surrounded by an eccentric cylinder of larger radius, refer to Table 5.4 in the book 'A Heat Transfer Textbook' by John H. Lienhard IV and V (Phlogiston Press 2008) or to table 3.5 in the book 'Heat Transfer - A Practical Approach' by Yunus A. Cengel (2014). It is assumed that the cables are in the duct so that it comes to contact.$\frac{U_d}{1+0.1\left(V_d+Y_d \theta_{dm}\right) D_{eq}}$ | Default |
$\frac{\rho_{d,fill}}{2\pi} \cosh^{-1}\left(\frac{{Di_d}^2+{D_{eq}}^2-\left(\frac{Di_d}{2}-\frac{D_{eq}}{2}\right)^2}{2Di_d D_{eq}}\right)$ | Bentonite filling, steady-state |
$\frac{\theta_e-\theta_{di}}{W_{conv,og}-W_{conv,gd}+W_{rad,int}}$ | Cables in riser |
$\frac{\theta_e-\theta_{di}}{W_{conv,int}+W_{rad,int}}$ | Cables in riser acc. Chippendale |
$\frac{1}{\frac{\pi D_{eq}}{1000} \left(h_{conv,int}+h_{rad,int}\right)}$ | Cables in riser acc. IEC 60287 |
$F_{\alpha} T_{4i}$ | buried inclined ducts |