2015 ME Graduate Student Conference April , 2015 STUDY OF RADIATION HEAT TRANSFER OVER A POWDER BED FOR SELECTIVE LASER MELTING PROCESS USING A MULTI-LAYER MODEL. Manish Patil M.S. Candidate Faculty Advisor: Dr. Shengmin Guo ABSTRACT Use of the laser energy to melt the metallic and non metallic powders in order to build the components of different shapes is a commonly used process nowadays in the industry. In Selective Laser Melting process (SLM), the energy transferred from the laser beam is utilized in melting of the metallic powdered bed. The interaction of laser bed and the powder metal becomes quite complicated because of an inhomogeneous and a porous nature of a powdered bed. Several attempts have been made to evaluate the Radiative heat transfer in absorbing emitting and scattering medium for a SLM process. In most cases, the previously developed models treat the bed as a bulk material [2 ] [3]. and assign the same physical properties throughout the depth of the bed. But in reality, the absorbed, the scattered, the emitted and the reflected laser beam interacts differently with the metal particles as it propagates further down into the powdered bed. When the depth of the bed is much greater than the wavelength of incident radiation, then treating the power bed as the homogeneous bulk material can no longer be accurate to capture the physics of the process. In our model, we segment the powder bed in to multiple homogeneous sub layers of very small thickness, and treat the individual layer with a different physical properties so that we can essentially go much closer to the realty. [see Fig. 1 ] In the typical process, the thickness of powdered bed is taken around 50 to 100 microns, the wave length of the monochromatic laser heat source caries from 1 to 5 microns. Radiation heat transfer in the porous bed is largely affected by the physical and optical properties of the material such as shape and sizes of the particles in the powdered bed, wavelength of incident radiation, absorbance, reflectance, scattering coefficients, refractive index and porosity of the bed which is a function of a depth. The famous radiative heat transfer equation for a emitting, absorbing and scattering medium written in the following form (eqn.1 ) (1) The equation gives us a change energy per unit volume when an incident radiation with an intensity propagates through an absorbing, emitting and a scattering medium with an observation direction and along the path (s). The gain or loss in the energy per unit volume is a summation of energy during emission, absorption and scattering processes which depends on the absorption ( and the scattering coefficients of the given material. The equation is simplified using which is a spectral extinction coefficient ( ) and is a spectral albedo. Fig. 1 Further, this integro-differential equation is solved for a one dimensional parallel case. Two flux method is effective in order to evaluate this simple case. This technique is also 39 used by Gusrov A.V. and his team for his model for a bulk material[3] [11]. The positive and the negative fluxes represents the incoming and outgoing radiation in a semi transparent slab. Our multi layer approach tracks down the path of individual ray as it travel in different layers of the slab. [See Fig. 2] This will generates the sets of connected linked integro differential equations for each layer. The semitransparent boundaries are considered for all inner sublayers. in order to solve these coupled equations. The final energy flux density is calculated by the sum of ∑ I+ and ∑ I -. 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