In this paper, a real-time mathematical heat transfer model for billet continuous casting of low carbon steel has been presented and solved by finite volume method. This model can be used to simulate the casting conditions which vary frequently. As taking the variation of superheat of liquid steel into consideration in the water flow rate distribution, the fluctuation of billet surface temperature has been decreased. Meanwhile the fluctuation of measured temperature has been largely reduced when it is measured with thermal imager. The mathematical model has been validated by measuring shell thickness and surface temperature in industrial caster. The on-line model can monitor surface temperature and shell thickness along the caster machine in the casting process, and it has been applied on the dynamic control system to adjust the operation parameters. The billet defect has been decreased greatly and the quality of billet has been obviously improved.KEY WORDS: real-time model; continuous casting; heat transfer; solidification; secondary cooling; dynamic control.......... (1) where T is the billet temperature, t is the time, x, y are the rectangular coordinates, k is the thermal conductivity of steel, c is the specific heat capacity of steel, r is the density of steel, and q is the latent heat source.Owing to the symmetry of heat transfer in square sections, one quarter of billet cross-section is selected as calculation area. The grid division and boundary conditions for cross-section of the billet are presented in Fig. 1. The P is the control volume, and w, e, n, s are the correspondence interfaces.In the time interval (t, tϩDt), Eq. (2) is obtained by finite volume method and the discrete equation group of complete implied format is formulated. 8,9) ...
Thermophysical Properties of SteelThe latent heat is generated during phase change between liquidus and solidus temperatures of steel and is ex- where L is the latent heat of fusion, r is the density of steel, f s is the solid fraction in the mushy zone and it can be expressed in accordance with Eq. (4) Equations (4) and (1) giveThe f s 3) of low carbon steel can be expressed by the following equation:... (6) where T L is the liquidus temperature of steel, T S is the solidus temperature of steel.The convective heat transfer in the liquid pool and mushy zone is quite difficult to be calculated by using differential equations. The effective thermal conductivity is given by the following linear relationship 5) :where k eff is the effective thermal conductivity, k is the thermal conductivity of solid steel, A is a constant, and f s is the solid fraction in the mushy zone.The specific heat capacity and density are expressed by the following equations: where sub-indices S and L, respectively, indicates solid and liquid state.
The Boundary Conditions (1) Initial ConditionThe boundary condition to the steady state casting has been assumed to be the same as the pouring or casting temperature (T 0 ) of the steel. (10) where T 0 is the steel casting temperature, which is ...