5.1. Analysis of the Filling Behavior of Semi-Solid Billet for the Thin-Wall Phone Cover
The velocity distribution of the semi-solid billet of the mobile phone shell during the thixotropic extrusion forming process at different displacements of the top mould with the billet temperature of 630 °C, mould temperature of 400 °C, and extrusion speed of 10 mm/s is shown in
Figure 4. It was found that the filling speed of the semi-solid material at the side edge was relatively high while that at the end edge was relatively low when the displacement of the top mould was 0.25 mm. This was because the semi-solid material in contact with the top mould began to flow to the side edge under the mould displacement. Therefore the upward squeeze filling effect was first observed at the side edge of the mobile phone shell due to the short material flow distance. However, the relatively few semi-solid materials were being squeezed at the end edge of the mobile phone shell due to the long flow distance. The lowest felling speed was observed at the corners of the mobile phone shell due to the relatively small amount of the semi-solid materials occupied there.
The distribution of filling velocity at the top mould displacement of 0.5 mm is presented in
Figure 4b. Similar to the displacement of 0.25 mm, the filling velocity of the semi-solid material at the end edge was lower than the side edge, which was higher than the corners. The highest velocity was located at the side edge near the symmetric line X, which was indicated by yellow vector arrows. When the displacement of the top mould was 0.75 mm, as shown in
Figure 4c, the semi-solid material started to flow into the corner region of the phone shell when it flew to the side edge region forced by the top mould. The reverse flow with a low speed was observed at the side edge near the symmetric line X, which is indicated by blue vector arrows. This means that the filling of the semi-solid material at the side edge has been finished. As presented in
Figure 4d, when the displacement of the top mould was 1 mm, the shape outline of the mobile phone shell is clear. The flow velocity at the side edge and corner was low, which was illustrated by the blue vector arrows. This means that the filling of the phone shell had been successfully completed at the displacement of 1 mm.
The load-displacement curve of the thixotropic extrusion forming under different displacements of the top mould at the billet temperature of 630 °C, die temperature of 400 °C, and the extrusion speed is 10 mm/s is shown in
Figure 5. It was found that the load of the top mould at all directions first increased rapidly, then slowly reduced, and gradually rose at the end. This variation phenomenon can be explained by the thixotropic extrusion deformation mechanism of semi-solid materials. The mesh formed by solid grains was gradually broken at the beginning of extrusion during the thixotropic extrusion process of high solid fraction semi-solid materials. Therefore, plastic deformation is the major mechanism at this stage. The liquid phase can then flow out when the solid grain is deformed, so the plastic deformation of semi-solid materials included the grain sliding and partial rotation of solid grains. Consequently, the required load for the deformation was reduced under the same conditions. However, as the reaction force of the shell edges on the top mould increased during the extrusion process, the increase in mould load was observed with the further elevation in the displacement of the top mould. Although the top mould born the load from all X, Y, and Z directions, the load in the X-axis and Y-axis directions was far less than the Z-axis. Therefore, the load at Z-axis was the main load for the top mould. The displacement of the top load where the rise of the load started due to the reaction force the shell edges at X-axis was observed lower than Y-axis, which is amplified and shown in
Figure 4. This was because the extrusion filling process at the side edge occurred prior to the end edge due to the unequal lengths, which caused different flow distribution at the end and side edges. Although the load at Z-axis was observed with the rising trend when the displacement of the top mould was higher than 0.5 mm, the deformation resistance was small as the billet is in the semi-solid stage. Therefore, the maximum load at the Z-axis during the thixotropic extrusion forming process was lower than 6.5 kN.
The temperature distribution of the billet processed by the thixotropic extrusion under different displacements of the top mould at the billet temperature of 630 °C, die temperature of 400 °C, and the extrusion speed of 10 mm/s is shown in
Figure 6. It can be found that the temperature at the edges was all higher than the main body of the mobile phone shell at all different displacements of the top mould. The temperature at both edges and main body reduced with the increase in the displacement. The temperature decrease in the main body was observed faster than the edges as it directly contacted the top mould during the extrusion process. When the displacement was 0.25 mm, although a decrease in the main body of the shell was observed, the temperature at edges maintained high. When the displacement was 0.5 mm, the temperature at outside surfaces of the main body contacting with the top and bottom moulds reduced to around 618 °C. At the displacement of 0.75 mm, the temperature at the outside surfaces of the main body dropped to about 612 °C, where the solidification was observed. However, the temperature at the inside space of the main body was still in the semi-solid temperature range. As the displacement of the top mould increased to 1 mm, the solidification of the main body of the mobile phone shell was finished while the temperature of the material at the end side and corner was still in the range of 612–618 °C, due to the late filling. This means that under these process parameters of the semi-solid thixotropic extrusion forming, the solidification of the main body has been finished at the end of the filling process while the temperature at the end edge and the corner were still above the solidus temperature, which is conducive to the sequential solidification of the phone shell.
5.2. Effects of Billet Temperature on the Solidification Behavior
The equivalent stress distribution of the mobile phone shell processed by the thixotropic extrusion at different billet temperatures under the mould temperature of 400 °C and extrusion speed of 10 mm/s is shown in
Figure 7. It was found that the equivalent stress reduced with the elevation in the billet temperature. The maximum equivalent stress was 10.6, 9.64, and 9.03 MPa at the billet temperature of 625, 630, and 635 °C, respectively. The reduction in the equivalent stress was relatively large when the billet temperature increased from 625 to 630 °C. It means that increasing the billet temperature is helpful to reduce the pressure required to form the mobile phone shell during the thixotropic extrusion process. Therefore, the relatively high temperature of the blank can be designed for reducing the deformation resistance. However, the billet temperature cannot be designed too high in order to obtain the qualified microstructure and clamping strength during the semi-solid thixotropic extrusion process.
The temperature distribution of the mobile phone shell processed by the thixotropic extrusion at different billet temperatures under the die temperature of 400 °C and extrusion speed of 10 mm/s is presented in
Figure 8. It can be seen that although the temperature of the phone shell elevated when the billet temperature increased during the thixotropic extrusion process, the variation of the temperature was not significant. This was mainly because, the volume of the semi-solid material was small compared to the mould, which caused a sufficient heat exchange between the mould and the semi-solid material. Consequently, no significant temperature change was observed when the thixotropic extrusion was finished. However, when the billet temperature was 625 °C, the minimum temperature of the mobile shell was found as 595.35 °C as shown in
Figure 8a, which is much lower than the solidus temperature of the aluminum alloy 6063 (610 °C). This low-temperature area was observed in the side edge, which would be harmful to the successful forming of the phone shell.
5.3. Effects of Mould Temperature on the Solidification Behavior
The equivalent stress distribution of the mobile shell processed by the thixotropic extrusion at different mould temperatures under the billet temperature of 630 °C and extrusion speed of 10 mm/s is shown in
Figure 9. It was found that the equivalent stress reduced with the increase in the mould temperature. The maximum equivalent stresses of the mobile phone shell parts were 10.9, 9.64 and 8.96 MPa at the mould temperatures of 350, 400 and 450 °C, respectively. The decrease in the equivalent stress from the mould temperature of 350 °C to 400 °C was observed more significant than that from the mould temperature of 400 °C to 450 °C. This means that increasing the mould temperature is able to reduce the pressure required for forming during the thixotropic extrusion molding process.
Figure 10 shows the load-displacement curve of the top mould during the thixotropic extrusion at different mould temperatures under the billet temperature of 630 °C and extrusion speed of 10 mm/s. It was found that the load of the top mould reduced with the elevation in the mould temperature. The load of the top mould was obtained as the maximum value in the load-displacement curve, which was found at a displacement of less than 0.1 mm. From
Figure 10, it can be observed that the load of the top moulds are 6.5, 6.1, and 5.9 kN at the mould temperature of 350, 400, and 450 °C, respectively.
Figure 11 shows the temperature distribution of the mobile phone shell processed by the thixotropic extrusion at different mould temperatures under the billet temperature of 630 °C and extrusion speed of 10 mm/s. It can be found that the general temperature of the phone shell elevated with the enhancement in the mould temperature. The temperature of the semi-solid material at the edges was higher than the main body in all mould temperature cases. As shown in
Figure 11a, most of the side edge temperature of the phone shell was below 615 °C when the mould temperature was 350 °C, which may lead to a high-temperature solid forming rather than the semi-solid forming. Therefore, the mould temperature is recommended as 400 °C or higher for a successful semi-solid forming of the mobile phone shell.
5.4. Effects of Extrusion Speed on the Solidification Behavior
The equivalent stress distribution of the mobile phone shell processed by the thixotropic extrusion at different extrusion speeds under the billet temperature of 630 °C and a mould temperature of 400 °C is shown in
Figure 12. It was found that the equivalent stress decreased with the elevation in the extrusion speed. The maximum equivalent stresses were 17.1, 9.64, and 6.64 MPa at the extrusion speed of 5, 10, and 15 mm/s, respectively when the forming was finished. The reduction in the equivalent stress when the extrusion speed increased from 5 to 10 mm/s was larger than that from 10 to 15 mm/s. Therefore, the required pressure for forming the mobile phone shell can be reduced by increasing the strain rate, but a high strain rate also causes a high requirement on the performance of the forming equipment, so the design of the extrusion speed is determined by the forming equipment performance. It was also found that the most uniform distribution of the equivalent stress was observed at the extrusion speed of 15 mm/s. This means that the deformation resistance of the material was the lowest at the extrusion speed of 15 mm/s, which was beneficial to the material filling.
Figure 13 shows the load-displacement curve of the top mould at Z-axis during the thixotropic extrusion at different extrusion speeds under the billet temperature of 630 °C and mould temperature of 400 °C. It can be seen that the initial maximum load on the top mould increased when the extrusion speed rose in the semi-solid thixotropic extrusion forming process of the mobile phone shell, which means that requirements for the tonnage of the forming equipment were high at a high extrusion speed. However, when the displacement of the top mould reached 0.3 mm, the load of the top mould at the extrusion speed of 5 mm/s surpasses that at the extrusion speed of 10 mm/s, which further exceeded the load at the extrusion speed of 15 mm/s when the displacement increased to 0.4 mm. With the further growth in the displacement of the top mould above 0.7 mm/s, the maximum load of the top mould was observed at the extrusion speed of 5 mm/s while the minimum value was found at the extrusion speed of 15 mm/s.
The phenomenon mentioned above in
Figure 13 was because, with the increase in the top mould speed, part of the solid phase grain agglomerates in the semi-solid microstructure were destroyed by the stronger shearing effect, which promoted the release of the liquid phase wrapped by the agglomerates and increased liquid content inside the semi-solid material. Therefore, the filling process of the semi-solid material becomes easier at a higher extrusion speed due to the easier slid and rotation of the solid grains. Furthermore, there was a relatively large temperature difference between the billet temperature and the mold temperature during the semi-solid thixotropic extrusion process. The percentage of the semi-solid material that solidified due to the cooling of the mould reduced with the increase in the top mould speed, which was beneficial for the filling process.
It was also found that the load of the top mould at the Z-axis first reduced with the elevation in the displacement and then increased when the displacement further augmented at all three extrusion speeds. At the displacement of 1.0 mm, the load of the top mould increased to 5.8 kN at the extrusion speed of 5 mm/s while that elevated to 6.1 and 6.8 kN when the extrusion speeds were 10 and 15 mm/s, respectively. However, the turning points of the variation were different at different extrusion speeds. The increasing trend started at the displacement of 0.7 mm under the extrusion speed of 10 mm/s and 15 mm/s while that took place at the displacement of 0.4 mm when the extrusion speed was 5 mm/s. This means that under the same other operating conditions when the displacement of the top mould reached 0.4 mm at the extrusion speed of 5 mm/s, the cooling and solidification took place during the filling process, which led to the increase in the top mould load.
The temperature distribution of the mobile phone shell processed by the thixotropic extrusion at different extrusion speeds under the billet temperature of 630 °C and a mould temperature of 400 °C is shown in
Figure 14. It can be found that the general temperature of the mobile phone shell is augmented with the elevation in the extrusion speed. As shown in
Figure 14a, at the extrusion speed of 5 mm/s, the highest temperature of the phone shell was observed as 613 °C, which was lower than the solidus temperature (i.e., 615 °C). This means that the forming process of the mobile phone shell was turned into high-temperature solid forming instead of semi-solid forming. It is shown in
Figure 14b,c that the maximum temperature of the phone shell was 622.6 °C and 626 °C, respectively. This means that an appropriate elevation in the extrusion speed of the top mould can keep the temperature of the phone shell in the semi-solid temperature range so that the entire thixotropic extrusion process can be successfully completed in the semi-solid range. Based on the simulation results in this study, the extrusion speed is recommended as 10 mm/s or higher for realizing the filling process of the material at the semi-solid state.
5.5. Optimal Process Parameters for the Semi-Solid Thixoforming of the Thin-Wall Phone Cover
According to the analysis of
Figure 4,
Figure 5,
Figure 6,
Figure 7,
Figure 8,
Figure 9,
Figure 10,
Figure 11,
Figure 12,
Figure 13 and
Figure 14, the effects of the billet temperature, mould temperature, and extrusion speed of the top mould on the forming of mobile phone shells in the semi-solid thixotropic extrusion forming process can be summarized as follows:
(a) The equivalent stress of the blank decreased while the forming temperature augmented with the elevation in the billet temperature. Therefore, the elevation in the billet temperature was able to reduce the pressure required in the thixotropic extrusion forming process of the mobile phone shell. However, the growth in the billet temperature would inevitably cause the coarsening and growth of the semi-solid microstructure during the semi-solid thixotropic extrusion process. Hence, both the forming pressure and the semi-solid microstructure quality need to be considered in the determination of the billet temperature. According to the simulation results, when the billet temperature was 625 °C, the minimum temperature of the mobile shell was found as 595.35 °C as shown in
Figure 8a, which is much lower than the solidus temperature of the aluminum alloy 6063 (610 °C). This low-temperature area was observed in the side edge, which would be harmful to the successful forming of the phone shell. Therefore, the billet temperature is recommended as 630 °C or higher.
(b) The equivalent stress and the load on the top mould of the mobile phone shell decreased with the elevation in the mould temperature, which means that the requirements for the tonnage of the forming equipment reduced when the mould temperature augmented. According to the numerical simulation results, when the mold temperature was 350 °C, the temperature of the material at most of the shell edges was observed below 615 °C. This may lead to high-temperature solid-state forming instead of semi-solid forming. Therefore, to successfully realize the forming of mobile phone shell parts in a semi-solid state, the mold temperature is recommended to be 400 °C or higher.
(c) The equivalent stress in the blank reduced when the extrusion speed of the top mould elevated. A significant decrease in the equivalent stress was observed when the extrusion speed was augmented from 5 to 10 mm/s, which helped to reduce the pressure required to form the mobile phone shell, but it caused higher requirements on the performance of the forming equipment. Furthermore, the temperature of the phone shell increased when the extrusion speed of the top mould rose, which helped to complete the forming process of the entire shell at the temperature within the semi-solid range. According to the simulation results, when the extrusion speed was 5 mm/s, the maximum temperature of the phone shell during the forming process was 613 °C, which was lower than the solidus temperature of 615 °C. This caused a high-temperature solid forming of the mobile phone shell instead of the semi-solid forming. Therefore, the extrusion speed of the top mould is recommended as 10 mm/s or higher.
The effects of process parameters on the SSTEF of phone shells obtained from all simulations can be found in
Table 3. In summary, to save energy and reduce the production cost, the optimal process parameters for semi-solid thixotropic extrusion forming of mobile phone shell parts are the billet temperature of 630 °C, the mould temperature of 400 °C, and the extrusion speed of 10 mm/s.
The macromorphology and the microstructure at different sampling locations of the aluminum alloy 6063 mobile phone shell processed by the semi-solid thixotropic extrusion at the billet temperature of 630 °C, mould temperature of 400 °C, and the extrusion speed of 10 mm/s are shown in
Figure 15. It can be seen from
Figure 15a that the mobile phone shell was fully filled with clear outlines and smooth surfaces. There were no obvious macro defects such as cracks, mold sticking, entrainment, shrinkage, etc., indicating that qualified and relatively stable filling process of semi-solid materials under these optimal process parameters.
Figure 15c shows that although the solid grains at Position I of the phone shell were observed spherical, more obvious local liquid segregations were revealed in the microstructure compared to Positions II, III, and IV. The liquid phase content was more concentrated at the edges in comparison to the main body. This was mainly because the liquid phase was easy to flow to the edges of the phone shell in the initial stage of forming due to the excellent fluidity. It was also found that excellent semi-solid microstructure characteristics were observed at all sampling positions in the main body of the phone shell (Positions II, III, and IV).
These microstructure characteristics can be summarized as: (1) the solid grains were all small and nearly spherical; (2) the uniformity degree of the microstructure was relatively high, and the variation in the grain size was small; (3) no obvious solid-liquid separation was observed in the microstructure. Therefore, the microscopic morphology of the mobile phone shell can be maintained almost the same as the semi-solid material before the forming process.
To sum up, in the filling process of semi-solid thixotropic extrusion, the flow of the semi-solid material was mainly in the state of liquid phase wrapping the spherical solid grains. However, at the edge position of the filling product, the local liquid phase segregation would take place due to the prior flow of the liquid phase. Moreover, the rotation and sliding of solid grains are also accompanied by the filling process. Less liquid phase segregation was observed in the packing stage after the filling process as the liquid phase that wrapped the solid grains was solidified under the pressure.
The average grain size and the shape factor of solid grain at four different positions in
Figure 15 are shown in
Table 4. The solid grains in the microstructure were small, uniform, and nearly spherical. The average grain size varied from 73 to 79 μm. in these four positions while the shape factor changed from 0.74–0.77.
The lowest grain size was found at Position I while the largest shape factor was observed in Position III. The highest average grain size and the lowest shape factor were found at Positions IV and I, respectively. Therefore, the average grain size of the microstructure for the whole product was then obtained as 76.92 μm and the shape factor was found as 0.76.