Three geometrical features of the die are most relevant for the active material flow and the process forces during plastification, extrusion and deposition, see
Figure 2: the topography of the inner and outer circular faces of the die and the geometry of its extrusion channels. For investigating their respective effects, seven different tool design variants were assessed, based on two main extrusion hole shapes, a "bowtie" and a "tri-hole" design. One important aspect of extrusion hole design was the inclination of the holes with respect to the vertical axis of the die (0, 15 or 45 degrees). An illustrated summary of the basic designs (# 1 and # 2) and all their variants is presented in
Figure 5, and
Table 1 summarizes the die designs.
5.1. Evolution of Tool Design
The first stage tested the original die designs # 1 and # 2, and determined that only a thin layer of feedstock was plasticized against the inner surface of the die. The dies scraped this extrudate off the end of the feedstock as a continuous ribbon, as shown in
Figure 6 on the left. In order to enhance this scraping effect, two new tri-hole die designs (# 3 & # 4) were created where the holes were machined at an angle to to the surface of the die to provide positive rake to the holes, see
Figure 6 on the right.
Dies # 3 and # 4 showed a clearly improved material throughput, and an improved layer consolidation during deposition. This resulted directly in greater bead width and thickness capabilities. The increased deposition rate of these tools also allowed for deposition lengths of 750 mm although the feedstock would still eventually bind in the lower end of the guide tube. After die designs # 1, # 2, # 3 and # 4 had been tested, both the guide tube end and die shape were revised. The target was to reduce the amount of material overflow to the sides which occurred, especially during failed trials, which resulted in extensive cleaning of the equipment. To do so, the relief taper was changed from a square to a circular profile. Also, all subsequent die designs included more extensive geometrical features on the inside to capture and guide the material flow towards the extrusion holes. An illustrated description is provided in
Figure 7.
Dies # 5 and # 6 were both based on the tri-hole design and added a feature to the center of the inner surface. This was done in an attempt to increase the thickness of the plasticized zone above the die and to guide the material directly to the three extrusion holes. This should have improved the deposition rate and reduced the force on the feedstock. For die # 5 the feature was a smooth cone 1.3 mm high, and for die # 6 the feature was a stepped pyramid 2 mm in height. The scrolls on the inner face were replaced by deeper scoops for improving the flow into the extrusion holes. Additionally, scrolls were added to the outer face of the die to encourage a more extensive consolidation of the bead and to improve heat generation while keeping forces on the substrate low. Die # 7, the final design of this study, was based on the bow-tie extrusion hole design. It also featured scoops on the inner and scrolls on the outer face of the die for the reasons stated above. Compared to the base design # 1 it also featured a larger extrusion hole, to align better with the size of the feedstock and the changes for guide tube end and die shape described in
Figure 5.
5.2. Quantitative Results for Tool Designs
During each deposition run various parameters were logged, such as spindle torque, feed force, substrate force, tool temperature, etc. at about 50 Hz. Post-deposition analysis of these log files enables quantitative comparisons of elements of the die performance.
5.2.1. Process efficiency and Process window
An important quality characteristic of each die design is the specific energy required to deposit material as referenced earlier, see Equation 8. Dies that require less energy per amount of material deposited are more efficient, and are probably more effective at transporting material through the die.
Figure 8 gives an overview of the specific process energy consumption and volumetric deposition rate for all die designs. In the figure, only deposition runs longer than 40 seconds were included, ensuring that die and process parameters were capable of maintaining the deposition process. The first 30 seconds and the last second of each log file were trimmed to ensure steady-state values.
Examining
Figure 8, the specific process energy consumption is shown to be inversely correlated with the deposition rate in general. That is, as the deposition rate is increased, less energy is needed to deposit the same material volume. Reviewing Equation 8,
and
have to scale linearly with
assuming the same processing conditions, however
will largely scale with time and more or less independent of the deposition rate. Together, this leads to the
curve shown, and the magnitude of the effect shows that
becomes a significant fraction of the process energy, especially at lower deposition rates. Furthermore, it is clear that, with increasing volumetric deposition rate, the curve flattens out. This is because a minimum amount of energy is needed to establish AFED’s working principle, i. e. heat up, deform and deposit a specific amount of material.
From
Figure 8 it is also clear that the efficiency of the various dies differs significantly. In particular, the initial designs # 1 and # 2 were not as capable of higher deposition rates and process efficiencies as the later designs # 3, # 4 or # 7. However, two of the later die designs # 5 and # 6 were found to be rather inefficient.
Two design factors can be identified and differentiated for this discussion: the ratio/area of the extrusion channel and the use of active material flow structures for extruding the feedstock.
As an example of the impact of active material flow structures, a direct comparison of dies # 2 and # 3 is useful. The only difference between the two is the active material flow structure implemented by an angle of the extrusion channels of 15 ° for die design # 3, see
Table 1. As seen from
Figure 8, the implementation directly enhances the process window and the efficiency compared to the original die design. This impact is confirmed when comparing the designs # 3 and # 4 with 15 ° and 45 ° respectively: they both show a very similar capability and efficiency, although die design # 4 has over 30 % more extrusion channel area.
To discuss the impact of larger extrusion channels, a comparison of designs dies # 5 and # 6 with die # 3 is instructive. While having extensive inner and outer structures, dies # 5 and # 6 do not perform as well as the less structured design of die # 3. This is clearly because, with # 5 and # 6 have only half the extrusion hole area (42 mm²) of die # 3 (85 mm²), leading to a bottleneck and high forces inside the tooling, as described in the next section. However, it should be noted that, due to the effect of active material flow structures, the performance of dies # 5 and # 6 is comparable to die design # 2 which has almost twice the extrusion channel area (but no angle). The most capable die design of this work with regard to deposition rate, die # 7, incorporates both: extensive inner and outer active material flow structures and a large area for the extrusion channel.
5.2.2. Feedstock forces
Another good way to evaluate different tool designs and their ability to provide an efficient AFED process is to compare the inner forces required to achieve a given deposition rate. As described earlier, one of the ultimate goals of AFED is to reduce the forces acting on the substrate to a minimum. While the plasticizing and heating forces should ideally be fully compensated within the tool, it is still beneficial to keep these forces as low as possible: High forces can cause excessive overflow, rod bending, and die clogging, and are a clear sign that the material is not being processed and extruded efficiently by the tool. In addition, the machine’s force capabilities are limited.
While the external deposition forces are heavily influenced by process parameters or conditions such as the chosen layer height, part geometry etc., the internal forces are more or less constrained by die geometry and the interaction of the die, guide tube and feedstock.
Figure 9 gives an overview of the rod forces for the seven die designs and different deposition rates. In comparison to the specific process energy consumption, a more clearly differentiated picture between the individual dies is evident. The rod force values of the individual dies tend to be grouped together (with varying scatter), which supports the conclusion that there is a die-specific force level in the steady state for each die that is almost independent of the deposition rate.
It is also noteworthy that there is a clear tendency for dies with larger extrusion channels or more extensive geometric structures to have lower rod forces. For example, dies # 1 (95 mm² channel area), # 2 (85 mm²) and # 3 (88 mm²) show significantly lower forces, averaging around 15 kN, than dies # 5 and # 6 (both 42 mm²) which typically exceed 18 kN. This effect can be directly related to the reduction in the cross-sectional area of the flow channels, resulting in a higher pressure required to force the material through the die to achieve a comparable deposition rate.
It is also noteworthy that die # 4 has significantly lower rod forces than die # 7 (on average 12.5 kN to 16.5 kN) despite the fact that die # 7 has approximately 40 % more extrusion channel area (# 4: 88 mm², # 7: 124 mm²). This can be directly attributed to the material flow enhancing structures for vertical transport in the outer/substrate direction, which # 4 has but # 7 does not. The effect of these flow structures can be quantified using the design evolution of dies # 2, # 3, and # 4:
Die # 2 with three holes but no active material transport to the outside requires just over 15 kN on average. Die # 3 has a 15 ° angled flow enhancing structure which reduces the force by approximately 0.5 kN, and # 4 with a 45 ° structure has the force reduced by approximately by 2.5 kN.
5.2.3. Substrate forces
Ultimately, the most relevant criteria for AFED from a manufacturing perspective are the outer forces of the process acting on the substrate during deposition. With perfect compensation of all the forces required to heat and plasticize the feedstock within the tool, the only forces acting on the substrate would be from the material flow to the outside and onto the substrate. By adjusting parameters such as layer height, spindle speed, or channel geometry, these forces could be kept to the minimum required for bonding to the substrate.
Figure 10 gives an overview on the force on the substrate by die number and volumetric deposition rate. Examining the average substrate force over all dies (which have the same outer diameter), an almost linear relationship between deposition rates and forces can be identified. This relationship is in good accordance with other solid-state processing technologies such as Friction Stir Welding (FSW). At deposition rates below 100 mm
3/s the force on the substrate is mostly kept below 2 kN, at 200 mm
3/s mostly below 4 kN etc. Averaged over all tools, this gives a slope of just over 20 Ns/mm
3, which can be interpreted as the impulse required to deposit one cubic millimeter of material on the substrate. This relationship can also be used to make statements about the process and local conditions: Since all dies have the same outer diameter and only successful depositions were considered, it can be concluded that this relationship follows the specific minimum thermo-mechanical process impact required for bonding to the substrate. As the local temperatures during the deposition runs were very homogeneous, this can be further reduced to the minimum mechanical process impact, i. e. the local contact pressure.
When comparing the substrate forces of the different die designs, it is striking that the two most efficient designs in terms of deposition rate, dies # 4 and # 7, are at similar levels despite their significantly different geometries. Die # 7 shows slight advantages in terms of throughput and die # 4 in substrate forces. The latter is particularly interesting as die # 4 had already shown lower internal (rod) forces than # 7. The additional advantage for external forces can be attributed to the small direct passage in the center of die # 7, which allows a portion of the rod force to act almost directly on the substrate. This is not the case with die # 4, where the 45 ° angle of the extrusion channel does not allow direct passage, but creates an additional vertical force component dependent on spindle speed. In this context, a direct comparison of dies # 3 and # 4 is again useful. As mentioned, the only difference between the two dies is the angle of their extrusion channels, 15° and 45°.
The greater ability of die # 4 to reduce internal forces compared to die # 3 has already been described in the previous section. In this case the reverse is true: At less than 4 kN, die # 3 shows significantly lower substrate forces than die # 4, even at high deposition rates above 400 mm3/s. In contrast, at over 8 kN, die # 4 is about 100 % higher. Due to the small geometric differences, this effect can clearly be attributed to the respective and differently induced vertical force components of the two dies. It also highlights the usefulness of the AFED operating principle in reducing the force on the substrate and the direct exchange of internal and external forces.
In direct relation to die designs # 3 and # 4, there is another interesting circumstance. Although die # 2 was not capable to achieve higher deposition rates, the geometry (which has neither a small direct passage like dies # 1 and # 7 nor an actively induced vertical material flow like dies # 3, # 4, # 5 and # 6) reflects the extensive possibility of force reduction by AFED: for example, for a deposition rate around 100 mm3/s runs with less than 500 N substrate force can be found.
5.4. Material Flow Analysis based on macros
Figure 12 provides an overview of structure and microstructure of the sample build, featuring the upper 14 layers. From the section shown, it is clear that layers are fairly uniform with a homogeneous thickness and a similar microstructure. The individual layers can be clearly distinguished from each other and are macroscopically well consolidated. With similarities to Friction Stir Welding (FSW) [
12], the side where the traverse and rotational velocities are in the same direction (advancing side, left) demonstrate a more extensive material flow than the retreating side (right), where velocities are opposing. Consequently, and in line with FSW, the advancing side is much more sharply defined than the retreating side, which has a much rougher outer surface. This rougher outer surface is also associated with the presence of voids on the retreating side. These voids are embedded between banded, wavy and periodic flow structures. These banded material flow structures are well known from the material flow characteristics of the FSW process [
13].
Examining any layer in isolation, it is evident from the microstructure that the lower half of each deposited layer is not as strongly intermixed as the upper half. Some "cold shuts" and voids are visible in some of the layers’ lower half at the transition to the preceding layer, again, mostly on the retreating side.
Figure 13 provides a detail highlighting this. This can be attributed to the fact that this upper half is in direct contact with the spinning die during deposition and thus experiences higher levels of post-extrusion mechanical mixing, shearing and thermal impact.
The longitudinal sections confirm the analysis of the transverse cross-sections: here it can be seen that the flaws and inhomogeneities occur mainly in layers which were created at the lower spindle speed level of 400 rpm, i. e. in every second layer of the build,
Figure 14 (right). In those layers banded structures of the periodic material flow are clearly recognizable especially in their respective lower half. In the layers in between, carried out at 500 rpm, the material flow is far better consolidated. Here, the individual banded structures can often not be distinguished and the overall process impact seems to be higher and more suitable for joining to the preceding layer.
Another characteristic of the AFED process can be recognized from the longitudinal sections. Analogous to friction stir welding, a periodicity of the material flow can be identified in the layers, as shown in
Figure 14. Banded structures as found in the layers in
Figure 14 created with a spindle speed level of 400 rpm show a medium spacing
d of about 1.42 mm. This corresponds well to what is to be expected from the 2-fold symmetry of the tool’s extrusion channels (bow tie), a 1092 mm/min traverse speed and the spindle speed:
It can be assumed, on the basis of the similarity to the FSW process that the variance in the spacing of the banded structures (ranging from 1.354 to 1.467 mm) can be attributed to the tooling run-out or the asymmetry of the tool geometry, e. g. the orientation of the extrusion channels relative to the substrate when depositing.
5.5. Mechanical Testing and Properties
Tensile tests for this study were performed according to ISO 6892-2:2018. Round tensile specimens measuring 5 x 25 x 51 were used (DIN 50125, Form B). All specimens were taken from the center of the layer and from the locations as sketched in
Figure 11. The aim was to test both for the strength within the layers as well as for the bonding between them, i. e. in the horizontal and vertical (build) direction. The tests were carried out 6 months after the build to avoid any significant influence from the precipitation kinetics of the alloy [
14].
Figure 15 shows the tensile test curves for the specimens. It can be seen that, within the elastic region and up to a plastic strain of some percent, specimens of both directions show a very comparable behavior: Specimens in the vertical direction, Y2 and Y3, both reach a yield stress of 138 MPa, and horizontal specimens X1 and X3 reach slightly higher values with 147 and 140 MPa. In the plastic region, the behavior begins to differ: Specimens in build direction (vertical) fail in a brittle manner at plastic strains of only around 5 % with ultimate tensile stresses of 189 and 185 MPa. Specimens along the layers (horizontal) show a significantly higher ductility of more than 20 %, reaching 213 and 212 MPa. The behavior of the material in horizontal direction corresponds closely to a T4 temper of the AA 6061 alloy, what is typical for extensive friction (stir) processing of age-hardenable alloys in T6 temper [
12,
15].
From the microstructural results presented earlier, the reason why the vertically oriented specimens experience brittle failure at lower stresses can be directly related to the flaws and inhomogeneities between the layers. With the onset of plastic deformation, the influence of internal notches becomes more relevant, acting as internal stress concentrators which leads to crack initiation. Due to the focus of this work on industrialization, process and tool design, and the fact that extensive fractographic investigations have already been carried out for AFED in a recent study [
6], a detailed fractographic investigation has been omitted at this point.