1 Introduction

Laser-based additive manufacturing (3-D printing) technology has been rapidly growing and finding applications in various industries including medical implants, automotive and aerospace parts with complex geometries and structures [1]. Specifically, laser powder bed fusion (L-PBF) processes such as direct metal laser sintering (DMLS™), selective laser melting (SLM™), LaserCUSING™, direct metal production (DMP™), and laser metal fusion (LMF™) have been receiving a lot of attention [2]. However, the build part quality and process performance, structural integrity, mechanical properties and related processing times are not at the desired industry-ready levels. Predictive process modeling and optimization for improved dimensional quality, product reliability, and overall productivity are of great interest to the current, ongoing research efforts [3,4,5,6,7]. This work gives a rapid calculation technique for predicting temperature profile and melt depth of metal powder material during laser melting. It uses pulsed laser heat source to acquire transient temperature behavior and enables studying the influence of process input parameters and powder material properties on the depth of melted material which is very practical for industrial applications.

Selective laser melting is an additive manufacturing process that directly and rapidly fabricates three-dimensional parts by focusing and fully melting metallic powders at selective locations and subsequently allowing for solidification. In laser melting process, the powder material is completely melted and solidified, as opposed to laser sintering processes where metal powder material is sintered, or partially melted [5, 8, 11]. Both groups of processes utilize similar operational set-ups typically requiring a high power fiber laser source, a beam delivery lens system, a scanning mirror, a metal powder supply, a recoater roller or blade, and a build platform, (see Fig. 1). When comparing laser melting to other manufacturing techniques, the L-PBF process has some clear advantages which can be listed as (1) high flexibility in manufacturing complex shapes, (2) quick process set-up avoiding the need for tooling, and (3) high suitability for product customization and use of different powder materials. These advantages allow for quick transition between manufacturing products of different geometries within the same station. The most attractive feature of laser powder bed fusion is the ability to use this process to produce highly complex geometries and structures that would normally not even be feasible using conventional manufacturing processes. However, laser melting has a major disadvantage: the laser heating process is known for its rapid heating times and unstable cooling times, which result in the formation of pores and voids in the microstructure, which often lead to reduced material density and loss of dimensional accuracy and process repeatability.

Fig. 1
figure 1

A common L-PBF process configuration [3]

2 Literature review

Temperature distribution possesses a significant factor in the resulting properties of the fabricated components using laser powder bed fusion or laser cladding processes. Therefore, accurately describing the temperature distribution during and after the process is vital to obtaining high-quality samples. The temperature distribution for L-PBF can be calculated using either an analytical solution approach or a numerical solution approach. Furthermore, a numerical solution can be obtained two-fold with a finite element analysis (FEA) approach, and by means of applying the finite difference method (FDM). L-PBF and SLS processes use powder material which has different thermal properties when compared to the bulk (fully dense) material. Gusarov et al. [9] established a model to calculate the thermal conductivity of a powder bed based on the molecular structure of the powder. Kolossov et al. [10] formed a thermal model of SLS utilizing finite element method by combining non-linear effects of conductivity and capacity and were able to confirm their results by means of experimental testing on titanium powder material. Patil and Yadava [11] analyzed the effect of laser processing parameters (power, beam size and hatch distance) on the temperature of a single powder layer under SLS and utilized a finite element approach to obtain temperature gradient variations on titanium powder material. Gusarov et al. [12] continued their investigations into SLM by developing a finite element model to analyze the influence of laser scan speed. They concluded that a scan speed range can be found where re-melted lines due to laser scanning are obtained as uniform. Non-uniform lines are undesirable due to their lowered mechanical properties, in what is known as the “balling” effect. Van Elsen et al. [13] provided analytical and computational solutions to the heat equation for moving point and semi-ellipsoidal heat sources. Roberts et al. [14] developed a 3-D finite element solution for computing the transient temperature results for several powder layers. They introduced a unique simulation technique in an attempt to reproduce the complexity created with considering several powder layers. Yin et al. [5] developed a simulation of the temperature distribution for laser micro-sintering (LMS). They analyzed the effect of laser power, beam size, scan speed on the temperature reached and the geometry of the melt pool. Finally, Song et al. [7] developed a FE simulation of the temperature profile to select process parameters in SLM. This group found that the temperature gradient from powder material bed’s top surface to the bottom surface is very large. Foroozmehr et al. [17] developed FE simulations considering optical penetration depth of laser in powder bed. Other researchers proposed thermal management systems for laser melting process [18]. In summary, the vast majority of the previous work in the calculation and analysis of the temperature distribution of laser additive manufacturing processes has centered in the development of finite element simulations. Additionally, most of the research efforts have focused on the effect of laser parameters in the process. Even though there are several different solutions presented in literature to the thermal analysis of laser melting processes [11,12,13,14, 16, 19,20,21] little attention has been given to employing analytical thermal modeling numerical solution using FDM analysis techniques, which are ideal for studying and simulating the effect of material properties, controlling and optimization of process parameters.

3 Materials and methods

Ti-6Al-4V is a titanium-based two-phase alloy which is very popular in manufacturing applications due to its corrosion resistance, high specific and mechanical strength, super-plasticity, low-weight, and biocompatibility, among many other properties. Its biocompatibility makes it a prime candidate for medical devices and implant applications and it is also widely used in aeronautical, aerospace and automotive applications for its high temperature strength. The compound composition of this material is given in Table 1 as reported by Sun et al. [4].

Table 1 Composition of bulk Ti-6Al-4V material

As explained previously, the biggest disadvantage of the L-PBF process is the difficulty in obtaining maximum possible density and favorable microstructure because of the fast rising temperature of metal powder and the cooling down effects that follow. In particular, the stability, dimensions, and behavior of the melt pool are the determining factors in the porosity and surface roughness of the resulting part. Furthermore, material’s physical properties e.g. heat capacity and thermal conductivity vary during the L-PBF process as the powder bed heats up. The temperature-dependent thermal properties of bulk Ti-6Al-4V are summarized in Table 2, as reported by Song et al. [7]. L-PBF of Ti-6Al-4V is a promising advanced manufacturing process because it has the potential to produce samples that satisfy the design requirements for medical device applications, such as complex internal channel geometries and dimensions, the creation of space gradual changing surfaces, and ultrathin walls as well as being suitable for orthodontic and orthopedic customization [3, 6]. Conventional manufacturing processes are not able to meet these requirements. Most of the existing studies on additive manufacturing of titanium alloys have focused on investment casting beginning with a 3-D printed master pattern, powder deposition, direct sintering or melting using lasers [8]. Additionally, many researchers have opted for the modeling route, attempting to model the L-PBF process and determine temperature profiles and distributions by solving heat transfer equations either analytically and/or numerically (with finite difference method and finite element method analysis).

Table 2 Thermal properties of bulk Ti-6Al-4V [7]

Powder density is a key material property for proper temperature analysis of laser powder bed fusion or laser cladding processes. Powders consist of a large number of very fine particles, whose small size allows them to be compacted or loosened into a wide array of densities. One way to model powder density is by considering it as a fraction of the bulk density [9, 14, 16]:

$$ \rho_{\text{powder}} \; = \;\left( {1 - \tau } \right)\rho_{\text{bulk}} , $$
(1)

where τ is the porosity of the powder material, indicating that at τ = 0 the powder is fully dense. The bulk density of solid Ti-6Al-4V is ρ bulk = 4.45 g/cm3. Therefore, by considering values of τ between 0 and 1, the effective density of Ti-6Al-4V powder can be expressed. As a result of this approach, powder material porosity becomes a process variable. Additionally, thermal properties of the powder material can be obtained from the bulk properties of the material by using the porosity of the powder where γ is a model coefficient specific to Ti-6Al-4V as given in [9, 14, 16].

$$ k_{\text{powder}} \; = \;k_{\text{bulk}} \left( {1 - \tau } \right)^{\gamma } . $$
(2)

One important aspect to note is that most researchers use different laser equipment and a different laser scanning strategy, depending on the resources available. Laser parameters, such as maximum power, wavelength, beam intensity distribution, and spot diameter have a direct influence in the L-PBF process. Additionally, the manner in which the process is conducted, namely the process parameters, will also affect the manufactured product. Important processing parameters include scanning velocity, hatching space, and scanning strategy (also referred to as scanning path) [4, 7].

In this paper, the effect of laser parameters in the temperature profile into the depth of powder material versus time is investigated. A temperature profile that shows the depth at which the powder will melt and later solidify with a single pulse can be obtained. By superimposing pulses as the laser heat source moves in the scanning direction, a complete profile of the temperature distribution can be obtained. Additionally, the temperature versus time is determined for a specific location in the powder bed. This will provide a better idea of the behavior of the melted powder pool as a function of time. The decision variables in this case will be the model inputs. These inputs can be both the laser parameters: laser energy, pulse duration, spot size diameter, and scanning speed, and the material properties such as the porosity, or density, of the powder. Once the temperature profile is obtained, the depth of melted material can be predicted, and compared against the desired level. By later applying process optimization techniques, it is possible to determine the variables which most affect the temperature profile, and therefore, the maximum depth of melted material. The model to obtain the temperature profile by solving the heat equation is based on finite difference method (FDM), which is presented next.

First, it was assumed that x represents the direction of the moving laser heat source, y is the direction orthogonal to x on the powder bed surface, and z is the direction into the powder material. Also, t will always refer to time unless otherwise noted. The general convection–diffusion equation is given by:

$$ \frac{\partial \rho u}{\partial t}\; + \;\frac{\partial \rho hV}{\partial x}\; = \;k\left( {\frac{{\partial^{2} T}}{{\partial x^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial y^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial z^{2} }}} \right)\; + \;\dot{q}, $$
(3)

where u is the internal energy (J), h is the enthalpy (J), ρ is the density (g/cm3), k is the thermal conductivity (W/cm K), \( \dot{q} \) is the heat source (W/cm3), T is the material temperature (K), and V is the velocity of the material in fluid phase (cm/s). In Eq. (3), the change in internal energy as a function of time and the convection are balanced with the heat conduction and the heat source. Given that du = dh = C dT, we can further simplify this expression by introducing the heat capacity, C (J/g K):

$$ \frac{\partial \rho CT}{\partial t}\; + \;\frac{\partial \rho CVT}{\partial x}\; = \;k\left( {\frac{{\partial^{2} T}}{{\partial x^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial y^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial z^{2} }}} \right)\; + \;\dot{q}. $$
(4)

Due to the rapid re-solidification nature characteristic of L-PBF, the velocity of the material in fluid phase is very small so it is assumed to be negligible (V = 0), so that the convection term drops out resulting in the well-known heat conduction equation. As given in Table 2, the material properties are a function of temperature, which yields:

$$ \rho \left( T \right)C\left( T \right)\frac{\partial T}{\partial t}\; = \;k\left( T \right)\left( {\frac{{\partial^{2} T}}{{\partial x^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial y^{2} }}\; + \;\frac{{\partial^{2} T}}{{\partial z^{2} }}} \right)\; + \;\dot{q}. $$
(5)

An accurate analysis can be obtained by accounting for the change in material properties due to the heating of the powder. Since the objective is to determine the depth at which the powder melts, only the temperature profile in the z-direction (depth) is considered. Heat conduction in the x- and y-directions is not considered due to the limitations that arise from attempting to solve 2D and 3D equations numerically [12, 13, 19, 21]. We solved the problem of heat conduction into the powder bed depth direction (z direction) and neglected heat conduction into the powder bed lateral and longitudinal directions (x and y directions). Therefore, it is assumed that conduction occurs principally in the z direction:

$$ \rho \left( T \right)C\left( T \right)\frac{\partial T}{\partial t}\; = \;k\left( T \right)\frac{{\partial^{2} T}}{{\partial z^{2} }}\; + \;\dot{q}. $$
(6)

To solve this equation numerically, we introduce the Crank–Nicolson scheme of the finite difference method. The heat equation is a member of the so-called parabolic partial differential equations. This type of equations can be solved using a Crank–Nicolson method which is based on central difference in space and the trapezoidal rule in time providing second-order convergence in time. When considering this 1-D case, the Crank–Nicolson scheme becomes a combination of the forward Euler method at time t = n and the backward Euler method at time t = n + 1. One key aspect of employing this approach is that for this particular type of differential equation, the Crank–Nicolson method is unconditionally stable. Therefore, very small time and space steps can be considered. For time-dependent derivatives, we utilize the forward derivative, so that the derivate of temperature at depth (z) with respect to time, at t = i, is given by:

$$ \frac{{\partial T_{z}^{i} }}{\partial t} \approx \frac{{T_{z}^{i + 1} - T_{z}^{i} }}{\Delta t}. $$
(7)

For the second derivative of temperature with respect to the spatial dimension, z, the Crank–Nicolson discretization is given by:

$$ \frac{{\partial^{2} T_{z}^{i} }}{{\partial z^{2} }}\; \approx \;\frac{{T_{z - 1}^{i} \; - \;2T_{z}^{i} \; + \;T_{z + 1}^{i} }}{{(\Delta z)^{2} }}\; + \;\frac{{T_{z - 1}^{i + 1} \; - \;2T_{z}^{i + 1} \; + \;T_{z + 1}^{i + 1} }}{{(\Delta z)^{2} }}. $$
(8)

Replacing Eqs. (7) and (8) in the simplified heat equation, Eq. (6), results in a finite difference formulation of the temperature profile:

$$ \rho \left( T \right)C\left( T \right)\left( {\frac{{T_{z}^{i + 1} - T_{z}^{i} }}{\Delta t}} \right)\; = \;k\left( T \right)\left( {\frac{{T_{z - 1}^{i} \; - \;2T_{z}^{i} \; + \;T_{z + 1}^{i} \; + \;T_{z - 1}^{i + 1} \; - \;2T_{z}^{i + 1} \; + \;T_{z + 1}^{i + 1} }}{{(\Delta z)^{2} }}} \right)\; + \;\dot{q}. $$
(9)

Solving for T(z) at time i + 1 gives the implicit equation:

$$ T_{z}^{i + 1} \; = \;T_{z}^{i} \; + \;\frac{k\Delta t}{\rho C}\left( {\frac{{T_{z - 1}^{i} - 2T_{z}^{i} + T_{z + 1}^{i} + T_{z - 1}^{i + 1} - 2T_{z}^{i + 1} + T_{z + 1}^{i + 1} }}{{(\Delta z)^{2} }}} \right)\; + \;\frac{{\dot{q}\Delta t}}{\rho C}. $$
(10)

The laser heat source is based off the Nd:YAG pulsed laser system [15] with a Gaussian-like laser beam that has a fundamental wavelength of λ = 1064 nm, a maximum pulse energy of E = 392 mJ, pulse duration of t p = 5 ns, pulse frequency f = 10 Hz and A = 0.25 cm2 spot area. For this simulation, a 5 × focused beam was considered, resulting in a spot size diameter of d = 1.90 × 10−2 cm. By varying the drive voltage, it is possible to modify and control the pulse energy. The laser intensity decays as it penetrates the material. This phenomenon can be modeled according to Beer-Lambert’s law as follows:

$$ I\left( {z,t} \right) = I\left( {0,t} \right)e^{ - \alpha z} , $$
(11)

where I(0,t) is the intensity at the surface (W/cm2) and α is the absorption coefficient (1/cm). The heat source \( S\left( {z,t} \right) \) is calculated by taking the negative of the derivative of the intensity with respect to the z direction while considering the effect of the material’s reflectivity to laser irradiation. It is assumed that a percentage of the laser energy, given by R, is reflected by the material. R is an optical property of the material and will change according to the laser wavelength. For Ti-6Al-4V at near-IR wavelengths, R = 0.75 [7, 16].

$$ {\dot{q}} = S\left( {z,t} \right) = \left\{ {\begin{array}{*{20}l} {\left( {1 - R} \right)I\left( {0,t} \right)\alpha {\text{e}}^{{ - \alpha z}} ,} \hfill & {\quad t \le t_{{\text{p}}} } \hfill \\ {0,} \hfill & {\quad {\text{o}}.{\text{w}}} \hfill \\ \end{array} } \right. . $$
(12)

Two approaches to determine laser intensity are considered. In the first approach we consider the ultra-short transient behavior of temperature rise. In this case, the laser intensity is calculated from the peak power of each pulse, given by:

$$ P_{\text{p}} \; = \;{\raise0.7ex\hbox{$E$} \!\mathord{\left/ {\vphantom {E {t_{\text{p}} }}}\right.\kern-0pt} \!\lower0.7ex\hbox{${t_{\text{p}} }$}}. $$
(13)

The peak intensity can be modeled using the Gaussian function for the corresponding Gaussian beam:

$$ I\left( r \right) = \frac{{4P_{\text{p}} }}{{\pi d^{2} }}{ \exp }\left( { - 2\frac{{r^{2} }}{{\left( {d/2} \right)^{2} }}} \right), $$
(14)

where r is the length from the any given point (x,y) to the laser beam centerline. To determine the intensity at the surface, I(0,t), in Eq. (11), we let I(0,t) = I(r). Then, the heat equation can be solved from the time when the pulse is fired (t = 0) to the moment right before the next pulse is fired. The next iteration of the problem is solved by recalculating I(0,t) based on the new distance r, using the previous temperature profile as the initial condition, then solving for the temperature distribution again. The process can be repeated until the laser has moved sufficiently away from the point of interest that I(r) is close to 0. It is clear that the total heat provided by the laser is then a function of the scanning speed. In this particular case, we will focus on the effect of a single pulse irradiation, assuming that r = 0. Figure 2 shows how peak intensity behaves as the pulse energy is modified.

Fig. 2
figure 2

Peak intensity during a single pulse width at the surface of the powder bed for three energy settings

Furthermore, the intensity profile can be obtained as a function of the depth by plotting Eq. (12) as given in Fig. 3. As expected, the powder material surface receives the laser heat greatly, with little to no heat from the heat source reaching to the bottom plate in the powder bed.

Fig. 3
figure 3

Peak intensity profile throughout the powder bed at the end of the pulse (t = 5 ns)

The second approach is to analyze the short transient behavior of temperature rise by considering the average energy delivered by laser. In this case, the average power is obtained from the laser energy by considering the pulse frequency of the laser, f, and can be given as:

$$ P_{\text{ave}} \; = \;E \cdot f. $$
(15)

The total time that a point of interest is subjected to this average power is determined from the scanning speed and the spot size diameter. Table 3 summarizes the relationship between scanning velocity, v s, and total time the point of interest is subjected to irradiation, t i , for d = 1.90 × 10−2 cm. It is clearly seen that a faster scanning speed corresponds to a shorter equivalent irradiation time. The latent heat of fusion in laser melting can be defined as specific energy per unit mass required for phase change from solid to liquid. This transformation occurs without a change in temperature, and occurs at the powder material’s melting point. For Ti-6Al-4V powder material, this latent heat is L f = 292 J/g [7] and the melting temperature is T m = 1933 K. There are several ways to incorporate the effect of the latent heat of fusion into the temperature model, either by using a temperature-dependent heat capacity term, or by adding an extra heat sink. The most common method is the apparent heat capacity method, in which a new heat capacity C app = C + C Lf is calculated. The heat capacity associated with the latent heat of fusion is given by:

Table 3 Irradiation time for varying scanning velocities
$$ C_{\text{Lf}} \; = \;\frac{{L_{\text{f}} }}{{T_{\text{l}} - T_{\text{s}} }}, $$
(16)

where T l (K) and T s (K) are the liquidus and solidus temperature of the material, respectively.

4 Results and discussion

Numerical analyses have been conducted in order to simulate the temperature profile into the depth of the powder material as well as transient of the temperature rise during pulse width. The 1-D heat conduction equation given by Eq. (4) was solved with Matlab®, using the Crank–Nicolson scheme presented in Eq. (8). The simulation code developed takes necessary inputs; physical, thermal, and optical properties of powder material as well as laser pulse energy, power intensity, and pulse width. Table 4 summarizes the thermal and optical material parameters used in this simulation. These parameter values are often used in modeling of Ti-6Al-4V powder material where average particle is considered about 25 μm in size. With respect to the numerical analysis of laser-powder material interaction using finite difference method implementation, the parameters given in Table 5 were utilized in the numerical analysis. The choice of simulation parameters, namely the time and space steps, was made based on the achieving proper convergence. The underlying assumptions of the model are (1) no heat loss during laser processing, (2) beam intensity follows a Gaussian profile, (3) powder material absorption is not depending on temperature. The initial and boundary conditions applied to solve the heat equation are \( T\left( {t = 0, z} \right) = 300 {\text{K}} \) (initial temperature is room temperature), and \( T\left( {t, z = D} \right) = 300 {\text{K}} \) (fixed temperature at the bottom of the sample).

Table 4 Physical, thermal, and optical material parameters
Table 5 Finite difference method parameters

The effect of laser energy and material density on the ultra-short transient temperature profile was analyzed. Table 6 shows how several combinations of pulse energy and powder density affect the maximum depth at which melting of the powder occurs. Figure 4 shows the temperature profile versus time at the powder material surface which has a certain percentage of the bulk density of solid Ti-6Al-4V. It can be seen that the temperature rises consistently from t = 0 to 5 ns, as the laser pulse acts on the powder bed. After the end of the pulse (t = 5 ns), no heat source acts on the powder bed. The melted material cools as the heat is conducted through the powder bed (Fig. 5).

Table 6 Simulation decision variables and resulting maximum melting depth of the powder
Fig. 4
figure 4

Temperature vs. time for a 50% dense, b 40% dense, c 25% dense Ti-6Al-4V at three different levels of laser pulse energy by using peak intensity as heat source

Fig. 5
figure 5

Temperature vs. depth for a 50% dense, b 40% dense, c 25% dense Ti-6Al-4V at three different levels of laser pulse energy by using peak intensity as heat source

It should be noted that there is a direct correlation between the maximum depth at which melting of the powder occurs and the maximum temperature, which very close to the surface. If the laser energy is increased indiscriminately, direct thermal ablation of the powder material occurs. Therefore, excessive temperature rise and subsequent burning can have adverse effects on the material. Utilizing a high-powered laser may cause gasification of the metal powder, which has adverse effects on part density. In the other hand, a low-energy setting may fail melt the powder depending upon the packing density as can be seen in Fig. 4a, b. It is possible to optimize the laser energy per powder area and volume so that only sufficient amount of melting is achieved Fig. 6 portraits the temperature profile along the depth of the powder bed at the end of the first laser pulse (t = 5 ns).

Fig. 6
figure 6

Ultra-short transient temperature vs. time at several depths for 50% dense Ti-6Al-4V by using peak intensity as heat source (E = 392 mJ)

Figure 6 portrays ultra-short transient temperature behavior as a function of time at three different depths. In Table 5, the maximum depth at which melting occurs had been identified at 3.25 μm. Figure 7 shows the sharp drop-off in maximum temperature for values of z larger than the maximum depth of melting.

Fig. 7
figure 7

Temperature vs. time for a 50% dense, b 40% dense, c 25% dense Ti-6Al-4V by using average intensity as heat source

It is clearly seen that higher temperatures are obtained when the porosity of the powder bed is increased. This is clear from Eq. (10), given that the density appears in the denominator. Reducing the density will result in an increase in the temperature gradient. Additionally, a more porous powder bed has a lower thermal conductivity as given by Eq. (2). Therefore, the powder bed will not cool as quickly when the powder bed density is lowered. The sum of these effects results in the temperature rise observed in Figs. 4 and 5. Additionally, the thermal conductivity of the material increases as the material heats up, accelerating the cooling process. The maximum time considered in the ultra-short transient simulation does not include the entirety of the cooling process, in which the temperature drops below the melting temperature, producing solidification, but rather focuses on the heating process due to the single-pulse heat source. The rapid cooling times result in material porosity and loss of dimensional accuracy, making process repeatability very challenging [16].

The effect of porosity in the short transient temperature behavior was analyzed. For this simulation, the pulse energy was modified to E = 196, 294, and 392 mJ with a constant frequency f = 10 Hz, resulting in an average power of P ave = 1.96, 2.94 and 3.92 W, respectively. The scanning speed was fixed at v s = 20 cm/s. Figure 7 shows the temperature profile versus time at the powder material surface (z = 0) for three different porosity values: 50, 45 and 25% dense powder bed. Finally, the short transient temperature behavior as a function of time at three different depths (z = 0, 10, and 20 μm) can be seen in Fig. 8.

Fig. 8
figure 8

Ultra-short transient temperature vs. time at several depths for 50% dense Ti-6Al-4V by using average intensity as heat source

5 Conclusions

In this paper, a representation of the temperature profile and melt depth in laser fusion of Ti-6Al-4V powder material was obtained. The temperature profile was numerically solved by using the finite difference method. Additionally, the maximum depth at which melting or cladding of the powder occurs was calculated. Several assumptions to simplify the model were made, such as the use of a single pulse stationary point heat source to obtain the ultra-short transient temperature behavior. With this model, it is possible to understand the influence of process parameters and powder density upon the temperature profile and the depth of melted, sintered or cladding material. In this particular simulation, pulse energy, average power, and powder bed packing density were selected as process decision variables. Through optimization techniques, the best laser and material properties can be determined for optimal laser fusion of metal powders. Material properties can be easily modified to represent other materials of interest besides Ti-6Al-4V.