1. Introduction
3D printing is a process that transforms 3D models produced from a computer-aided design (CAD) into physical objects. For the manufacture of 3D objects, a 3D computer model, software capable of processing the model, a machine or printer that uses 3D technology and the material to be used are required [
1].
There are seven classifications additive manufacturing (AM) processes [
2]: Extrusion of Materials (MEX), Vessel Photopolymerization (VPP), Powder Bed Melting (PBF), Binder Jetting (BJT), Material Jetting (MJT), Sheet Rolling (SHL), Directed Energy Deposition (DED).
AM refers to the production of physical objects from a computational model with the possibility of using different materials with complex geometries that were impossible for previous manufacturing technologies [
3,
4,
5,
6].
Within the MEX process, one of MA's technologies is filament fusion manufacturing (FFF). In this method, the thermoplastic filament is melted in the heating block, directed to the extruder nozzle and cooled again after leaving the nozzle. In this process, the material is deposited layer by layer until the object is made (
Figure 1) [
1,
7,
8].
To use this method, it is necessary to manufacture the filament. To do this, the pellets are melted and transformed into filaments, constituting a thermomechanical cycle before printing. In comparison, Fused Granule Fabrication (FGF) technology eliminates this cycle by directly utilizing the granular form (pellets).
FGF is a process in which the printer is fed directly into the pellets. The pellets are stored in a hopper and directed to screw extruder. In the screw, the material is melted in the heating block region and forced into the nozzle. After leaving the nozzle, the material is cooled, which is selectively deposited layer by layer until the object is completed (
Figure 2).
The use of granular material makes it possible to use more types of materials. In addition, it allows the mixing of elements directly in the extruder. It also avoids additional processes in the material while preserving the physical capabilities of the polymer [
7]. This method, compared to FDM, saves energy costs and the time used to manufacture the filament, making the material less expensive [
5,
6].
The extruder screw can deposit material up to two hundred times faster than in conventional printing technology [
6]. This allows the manufacture of products with greater volume, on a larger scale and in a shorter time.
FGF technology allows the use of many thermoplastic polymers, including ABS and PP. In 3D printing, the use of PP is a challenge because its crystallization causes thermal shrinkage, affecting the interfusion between the layers [
9]. In addition, another problem encountered with the use of PP in material extrusion (ME), is the low adhesion of the material on the printing platform [
10].
One way to promote the use of PP in 3D printing is the use of blends with other thermoplastic materials to reduce the problems in the use of PP in 3D printing. One of the hypotheses investigated in this research is whether the blend of PP and ABS would improve the behavior of the PP matrix during printing.
The blend between PP and ABS has already been studied by other researchers. K. Wang et al. [
11] used ABS as a β-nucleating agent (β-NA) to harden PP. To make mixture they used the melting mixing method, the materials were melted at a temperature of 180°C in the proportion of 80% PP and 20% ABS and mixed with a rotation of 60rpm for 8 min. The resulting material was transferred to a mold injection machine for the manufacture of the specimens, with a melting temperature of 180°C and a mold temperature of 40°C for 8 seconds.
A. C. Patel, R. B. Brahmbhatt, and S. Devi [
12] used PP-g-2-HEMA to make the PP blend compatible with ABS in different concentration proportions. To do this, PP and PP-g-2-HEMA were premixed in a 1:1 ratio in a simple extruder with four different temperature zones: 190-200-210-220°C. com a rotational speed of 50rpm. After that, the material was palletized and mixed with ABS in the same extruder with temperature zones of 200-220-230-225°C at 50rpm for PP-rich blends and 220-230-250-240°C for ABS-rich blends. The resulting mixtures were palletized and the specimens manufactured by injection molding.
C. Wang, Z. Zhang, Y. Du, J. Zhang, and K. Mai [
13] used a β-NA, PP and ABS to make blends of PP and ABS with several different concentrations. The blends were prepared in two different ways. The first one mixed β-NA, PP and ABS simultaneously in an HK-200 internal mixer with a temperature of 240°C and a rotation speed of 50 rom for 5 min. The second way was to first prepare the PP mixture with 5% of the weight of β-NA in a twin-screw extruder with a temperature of 190°C, the material was palletized and mixed in the internal mixer with ABS to make the blend.
G. S. Lohar and B. F. Jogi [
14] blended PP with ABS in concentrations of 80% PP and 20% ABS using a twin-screw extruder rotating in opposite directions. The temperature range used was 155-210-240°C with a rotation speed of 10rpm. The resulting material was transferred to an injection machine in an in-mold where the samples were molded at 220°C for 3 minutes.
A similar thing in the research cited is that first the material needs to be manufactured and then go through a molding process. Thinking about reducing the number of steps for the manufacture of blends and energy expenditure, it would be possible to use FGF 3D printing technology to unite the blending manufacturing process with the manufacture of inputs. The second objective of this work was to use FGF printing to reduce one of the stages of manufacturing the polymeric blend, aiming at the production of inputs with a lower energy consumption.