Jtam.dvi JOURNAL OF THEORETICAL AND APPLIED MECHANICS 49, 4, pp. 1019-1028, Warsaw 2011 IDENTIFICATION OF ALLOY LATENT HEAT USING THE DATA OF THERMAL AND DIFFERENTIAL ANALYSIS Bohdan Mochnacki Romuald Szopa Czestochowa University of Technology, Częstochowa, Poland e-mail: moch@imi.pcz.pl Thermal and differential analysis (TDA) is often used as a tool for qu- antitative estimation of solidification parameters of alloys (e.g. tempe- ratures corresponding to the beginning and the end of phase change, kinetics of latent heat evolution, etc). TDA system offers a possibility of observation of the cooling (heating) rate, which means that the course of derivative ∂T/∂t can be analyzed. In this paper, the identification of alloy latent heat on the basis of additional information resulting from TDA measurements is discussed. At the stage of numerical modelling, the finite difference method (FDM) is used, the examples of computa- tions are also shown. Key words: solidification process, latent heat identification, numerical methods 1. Introduction A typical TDA system consists of the following elements (Fig.1): • sample casting with thermocouple (1), • amplifier and derivative creator (2), • recording system and data presentation (3). The geometry of typical sample casting is close to a cylindrical one (Moch- nacki and Suchy, 1995), but in this place the other real shape of casting can also be considered, and the thermocouples can be located at the optional set of points from the domain considered. In Fig.2, an example of TDAmeasure- ments is presented (cast iron) (Kapturkiewicz, 2003). One can see, the course of TDA curves (cooling curve and its derivative) is a smooth one, and it is a 1020 B. Mochnacki, R. Szopa Fig. 1. TDA system Fig. 2. Example of measured TDA curves result of using additional numerical procedures at the stage of creation of the cooling curve and its derivative. The position of characteristic points A, B, C,... allows one to predict dif- ferent thermal andmechanical features of the castingmaterial, but these pro- blems will not be discussed here. The aim of considerations presented here is the identification of the alloy latent heat on the basis of information resulting fromTDAmeasurements. 2. Mathematical description of casting solidification The following energy equation is considered (Chang et al., 1992; Kapturkie- wicz, 2003; Majchrzak et al., 2008; Mochnacki and Suchy, 1995) c(T) ∂T(x,t) ∂t =∇· [λ(T)∇T(x,t)]+L ∂fS(x,t) ∂t (2.1) where λ(T) is the thermal conductivity, c(T) is the heat capacity, L is the volumetric latent heat, fS is the volumetric solid state fraction of a metal, Identification of alloy latent heat... 1021 T(x,t), x, t denote temperature, spatial co-ordinates and time, respective- ly. One can see that only conductional heat transfer is taken into account (the convection is neglected) – it results from the geometrical features and di- mensions of sample casting (Fig.2). In the case of more complex thick-walled castings and considerable rates of pouringmoulds (e.g. continuous casting), it is possible to apply equation (2.1), but in the place of real thermal conducti- vity of a molten metal, the so-called effective thermal conductivity should be introduced (see: Mochnacki and Suchy, 1995). Assuming the knowledge of function fS = fS(T) for the interval of tem- peratures [TS,TL] corresponding to the mushy zone sub-domain, one has ∂fS(x,t) ∂t = f ′S(T) ∂T(x,t) ∂t (2.2) Additionally, for T > TL : fS = 0 and for T < TS : fS = 1, it results from the definition of the function discussed. Introducing (2.2) into (2.1) one obtains [c(T)−Lf ′S] ∂T(x,t) ∂t =∇· [λ(T)∇T(x,t)] (2.3) or C(T) ∂T(x,t) ∂t =∇· [λ(T)∇T(x,t)] (2.4) where C(T) is the substitute thermal capacity (STC) of the alloy (Kaptur- kiewicz, 2003; Majchrzak et al., 2008; Mochnacki and Suchy, 1995). The soli- dification model based on equation (2.4) is called “a one-domain approach”, because the same equation describes the thermal processes proceeding in the whole, conventionally homogeneous casting domain. One can see that for the molten metal and solid state, the derivative dfS/dT = 0 and the substitute thermal capacity directly correspond to the volumetric specific heats of these sub-domains. One of the most popular approximation of fS(T) is the function of the form fS(T)= (TL−T(x,t) TL−TS )n for T ∈ [TS,TL], n> 0 (2.5) Formula (2.5) assures the compliance with requirements fS(TS) = 1, fS(TL) = 0. Let us assume the linear form of function (2.5). Then, for con- stant values of heat capacities cS, cL (liquid and solid states) one obtains an 1022 B. Mochnacki, R. Szopa approximation of C(T) in the form of a stair-case function (see: definition of STC – Eq. (2.3)) C(T)=          cL for T >TL cP + L TL−TS for TS ¬T ¬TL cS for T TL λP for TS ¬T ¬TL λS for T