Strojniški vestnik - Journal of Mechanical Engineering 56(2010)2, 93-103 UDC 621.785 Paper received: 19.11.2009 Paper accepted: 19.01.2010 A Simulation of the Quenching Process for Predicting Temperature, Microstructure and Residual Stresses Caner Çimçir1 - C. Hakan Gur2* 1 Stiftung Institut fur Werkstofftechnik, Germany 2 Middle East Technical University, Metallurgical and Materials Engineering Department, Turkey A finite element model capable of predicting the temperature history, evolution of microstructure and residual stresses in the quenching process is presented. Proposed model was integrated into Msc. Marc® software via user subroutines. Verification of the model was performed by X-ray diffraction residual stress measurements on a series of steel cylinders quenched. ©2010 Journal of Mechanical Engineering. All rights reserved. Keywords: steel quenching, simulation, finite element method, microstructure, residual stress 0 INTRODUCTION Quenching of steels is a multi-physics process involving a complicated pattern of couplings among heat transfer, phase transformations and stress evolution. Physical fields interact with each other either by sharing of state variables or coupling interactions. Because of the complexity, coupled (thermal-mechanical-metallurgical) theory and non-linear nature of the problem, no analytical solution exists; however, numerical solution is possible by the finite difference method, finite volume method, and the most popular one - finite element method (FEM). Heat transfer to the quenching medium is the driving physical event as it triggers other processes, and thus, quenching techniques are usually nominated as immersion quenching, spray quenching or gas quenching. Variation of temperature at any point in the component is the major driving force for phase transformations. Upon cooling, thermodynamic stability of parent phase is altered, which results in decomposition of austenite into transformation products. The transformation rate depends on the temperature and the cooling rate. On the other hand, there is a heat interaction with the surroundings during phase transformations. Phase transformations that occur during quenching are exothermic and they alter the thermal field by releasing latent heat of transformation. Thermal stresses are generated in the quenched component due to large temperature gradients and the variation of mechanical properties with temperature. Varying cooling rates at different points lead to varying thermal contractions which must be balanced by an internal stress state. Those stresses may cause a non-uniform plastic flow when their magnitude at any point exceeds local yield strength. On the other hand, since plastic deformations are relatively small (< 3%) in the quenched part, heat induced by plastic deformation is neglected. During decomposition of austenite into transformation products such as ferrite, pearlite, bainite and martensite, a volume increase is observed in the transforming region due to density difference between the parent and the product phases. Those strains are the primary source of fluctuating internal stress field, besides the thermal stresses and transformation induced plasticity (TRIP). It refers to the irreversible strains produced by the interaction of macroscopic stress and the microscopic plasticity due to phase transformations. In addition, stress and plasticity affect the phase transformations by altering both the thermodynamics and the kinetics of the transformation. Most commonly observed effect of stress on transformation diagrams is the shift of critical temperatures and times. In some cases, transformations may be induced or totally inhibited by stress. This concept is generally referred to as stress induced/inhibited phase transformation. During quenching, thermal and phase transformation strains co-operate and cause a continuously fluctuating internal stress field. In extreme cases, part could even crack. At any point in the quenched part, stress varies with time depending on the variation of thermo-mechanical properties with temperature and cooling rate. When the local yield strength is exceeded at some *Corr. Author's Address: Middle East Technical University, Metallurgical and Materials Engineering Department, Turkey, chgur@metu.edu.tr temperature at any point in the part, a nonuniform plastic flow occurs. A lot of research has been conducted to develop numerical simulation tools for prediction of final state of the component after quenching. The first studies on prediction of microstructure and residual stress distribution in quenching by computer simulation originate from the early 1970s. In the early 1980s, many studies for the implementation of phase transformation effects in the previously developed models were conducted. In the second half of the 1980s, many research groups developed improved constitutive models for material behavior during quenching of steels. The first mature models for the effect of stress on phase transformation and TRIP were developed. Previously neglected physical phenomena such as plastic memory loss during phase transformations, effect of stresses on the transformation thermodynamics and kinetics, transformation plasticity were implemented in the simulations. The theory of heat transfer during quenching, the selection of quenchant, and fundamentals of intensive quenching were presented. In 1990s, improvements in computational power and the finite element software lead to an acceleration in research; especially the concepts of calculation TTT and CCT diagrams and TRIP became more mature. Several commercial FEA software simulating quench processes became available. Since 2000, from the viewpoint of development of new technologies to control quenching, many articles and reviews have been published. Simulation of gas quenching and coupling quenching simulations with computational fluid dynamics (CFD) calculations have become a major interest. Currently, most of the research is focused on single phase gas quenching. Although CFD calculations still requires considerable amount of computational power, single phase calculations can be performed. These kind of simulations allow engineers to optimize of gas quenching system to minimize the distortion and to obtain optimum residual stress and microstructure distribution. However, the simulation of fluid flow during immersion quenching, which is the most common process in the industry, is not yet performed. The major drawback is quantitative description of thermo-physical events occurring on the surface during quenching. Extensive literature review about the simulation of quenching and thermal treatments can be found elsewhere [1]. This paper presents a 3-D FEM based model of quenching, which is integrated into commercial software Msc.Marc via user subroutines to predict temperature history, evolution of microstructure and residual stresses. 1 MODELLING 1.1 Heat Transfer Quenching can be defined as a transient heat conduction problem with convective and radiation boundary conditions with internal heat source and sink. Basically, heat is removed from the surface of the specimen by convective heat transfer to the quenchant and by radiation, which results in thermal gradients driving the conduction inside the component. The essential point in modeling of quenching is the addition of an internal heat source term into this equation. The origin of this term is the latent heat released by phase transformations. The transient heat transfer within the component during quenching can mathematically be described by an appropriate form of Fourier's heat conduction Eq. (1). Considering that the thermal field is altered by the latent heat of phase transformations, the equation can be expressed in its most general form as, p (T).c (T).^ = div(A(T).VT) + Qm (T,t) (1) dt where p(T), cp(T) and X(T) is the density, specific heat, thermal conductivity of the phase mixture given as a function of temperature and QTR is the latent heat release rate due to phase change. Thermal properties of the phase mixture is approximated by a linear rule of mixture, N P(T ) = 2 P Z k (2) 1 where P represents a thermal property of the mixture. Pk and Zk are a thermal property and fraction of kth constituent, respectively. To incorporate the effect of latent heat, a fictitious specific heat (Cp*) is defined as, c;=i h). z+i =c,+ž (3) where AHk is the latent heat of transformation for transformation of austenite into the kth phase. Then, initial and boundary conditions are set to complete the thermal problem definition. Initially all nodal temperatures are set to austenitization temperature. The surfaces in contact with the quenchant have a film heat transfer boundary condition with surface temperature dependant heat transfer coefficient in the form of: W(Ts, ) = h(Ts )(Ts - Tx ) (4) where Ts, Tm , y and h are surface temperature, quenchant temperature, heat flux and temperature dependant heat transfer coefficient, respectively. The use of a temperature dependent heat transfer coefficient allows simulation of different cooling regimes in different stages of quenching (vapor blanket, nucleate boiling, and convective cooling). Symmetry surfaces and surfaces which are not in contact with quenchant are assumed to be insulated surfaces by setting the heat flux to 0 as: Y = = 0 (5) dn where n represents the unit normal vector. 1.2 Phase Transformations Phase transformations can be categorized into diffusion controlled transformations and martensitic transformation, for which calculation of microstructural evolution requires different approaches. Since each point in the specimen has a distinct thermal history, the simulation of phase transformations requires mathematical models for anisothermal transformations. Different thermal paths will result in different amount of the product phase although all paths start and finish at the same temperature and time. Thus, both T and t can not be used as state variables. This realization introduces the notion of "additivity", which was first proposed by Scheil [2]. This concept was later extended to solid state phase transformation by Cahn [3], and generalized by Christian [4]. Additivity principle has long been discussed, reviewed and adopted by many authors [5] to [18]. General conclusion that can be drawn from these studies is that conventional Scheil-Cahn-Christian additivity principle is not quite accurate in the calculation of anisothermal kinetics from isothermal kinetic data. Some of the cited works improved the additivity principle to achieve a better fit with experimental data, however; most of these methods require additional experiments to be performed. The critical temperatures for phase transformations can directly be extracted from TTT and equilibrium phase diagrams or calculated using analytical expressions. In literature, there are several proposals: some of them are based on thermodynamic calculations, whereas the others are purely phenomenological expressions based on regression analysis. Kinetic parameters can be extracted from TTT and CCT diagrams or can be determined experimentally by measuring any property which is sensitive to phase transformations (such as volume, heat response, conductivity, magnetic permeability change etc.). Diffusion Controlled Phase Transformations Diffusion controlled transformations occur by an incubation period followed by a transformation stage. In order to calculate incubation time required for a diffusional transformation under anisothermal conditions, isothermal transformation diagram (IT) data and ScheiFs additivity principle is used. According to Scheil's additivity rule, if r(4, T) is the isothermal time required to reach certain transformed amount &, the same transformation amount will be reached under anisothermal conditions when the following Scheil's sum (S) equals to unity [2]: S - -Z Ati 1 T(šk T ) a (6) where At, , t are the time step size and isothermal time to reach 4 at the current time step. Next, growth kinetics needs to be calculated. After the incubation period (S = 1), anisothermal growth kinetics is calculated using a modified Johnson-Mehl-Avrami-Kolmogorov (JMAK) Eq. (7) and ScheiFs additivity principle [19]. Zj = zr Zr-zr )(l-exp((T).T";(T))) (7) where ZkJ , ZYJ are the volume fractions of kth microstructural constituent and austenite at current j) time step. Zk°, Zkmax are the initial and maximum fraction of kth microstructural constituent. t is the fictitious time calculated using the transformed amount in the previous time step by: Tj + - ln (l -1))(T) bk (T) (8) bk(T) and nk(T) in Eq. (7) are material constants that can be extracted from IT diagram by: ln [ln(1 -Z )/ln(1 -Qf)] nk (T) = ■ bk (T) = ln ( / tf ) - ln(1 -Ck) t nt (T) (9) (10) where Zs, Zf are the fractions of transformed phase at the beginning and at the end of the growth stage, which are generally 0.05 and 0.95, respectively. For proeutectoid ferrite tranformation, Zm™ can be calculated using lever rule on equilibrium phase diagram by: 0 z-ei ^ a Ae3 - T Ae3 - Aei e a ; T > Ae ; Aei< T