$$\rho c_p \frac{\partial T}{\partial t} = \nabla \cdot (k \nabla T) - \rho L \frac{\partial f_l}{\partial t}$$
相变化的热方程(焓法):\(L\) 融解潜热 [J/kg]、\(f_l\) 液相分率
$$\mathrm{Ste} = \frac{c_p (T_{wall} - T_m)}{L}$$
Stefan数:显热与潜热之比。Ste < 1 时潜热占优
$$s(t) = 2\lambda\sqrt{\alpha t}$$
Neumann解(半无限体):\(s\) 熔融界面位置 [m]、\(\alpha = k/(\rho c_p)\) 热扩散率