1. Introduction
Material extrusion additive manufacturing of high-performance thermoplastics such as PEEK (polyether ether ketone) or PEI (polyethyleneimine) has become a manufacturing process of choice for aerospace applications in recent years. Some approaches for aerospace applications pursued by the ESA (European Space Agency) are described by Lafont et al. [
1,
2]. Similarly, there have also been attempts to print CubeSat structures from PEEK [
3] or multifunctional satellite structures [
4,
5]. Further possible applications result from functionalising the 3D printable materials with various fillers [
6].
However, there are limits to using 3D printing in load-bearing structures in terms of performance and size. When printing PEEK, high process temperatures, especially nozzle, build chamber and build plate temperatures, are generally required to optimise the mechanical properties [
7]. Nevertheless, the mechanical properties remain below those of injection-moulded components [
7,
8].
One approach to overcoming these limitations is to produce hybrid structures by overprinting thermoplastic laminates. The outstanding mechanical properties of continuous fibre-reinforced laminates can be combined with the design freedom and functionalisation of 3D printing. Morales et al. [
9] presented a process in which the joint between PA 6 (polyamide 6) laminates and 3D printing is produced in situ during overprinting. Penter et al. [
10] and Maier et al. [
11] investigated in situ joining in more detail. The implementation of this process in an automated process chain was described by Matkovic et al. [
12]. Chauvette et al. [
13] describe how overprinting can produce functionalised body structures for aircraft. A similar large-scale approach using SEAM (Screw Extrusion Additive Manufacturing) was used by Atzler et al. [
14]. They have shown that the toolpath planning and its tolerances significantly affect the bonding quality during overprinting [
15]. Detailed investigations into in situ joining with aerospace-grade material PEEK were carried out by Caprais et al. [
16,
17] and Hümbert et al. [
18,
19]. They showed that, as with the printing of PEEK, high process temperatures are also required for in situ joining between PEEK 3D printing and PEEK laminate. Sufficient strength can only be achieved under certain conditions, and stable process control is therefore necessary. The properties of the joint can be traced back to the layer bonding, just like the layer bonding in 3D printing [
20]. A deep understanding of this layer structure is, therefore, the basis for the design of the process.
The influence of the process parameters on the mechanical properties of printed PEEK, and thus the layer bonding, has already been investigated in detail. Zanjanijam et al. [
7] concluded that both high nozzle temperatures and low gradients between the extruded material and the substrate are crucial. The study by Liaw et al. [
20] on bonding strength supports this conclusion. Wang et al. [
21] and Yang et al. [
22] observe a similar behaviour, also concerning crystallinity.
In addition to the experimental investigation of inter-layer bonding, modelling is a helpful tool for predicting mechanical properties and process design. The modelling includes material extrusion, fibre orientation, residual stresses and inter-layer bonding [
23]. Inter-layer bonding is generally divided into three phases: intimate contact, neck growth and molecular diffusion [
24]. Intimate contact and neck growth occur in the first material deposition phase. Neck growth was described by Bellehumeur et al. [
25] and Kallel et al. [
26] using a sintering model, whereby a good correlation between the model and measurement could be demonstrated. In Coogan and Kazmer [
27], the intimate contact and, thus, the neck radius were further described by the contact pressure.
After the neck growth, the inter-layer bonding is formed by diffusion. The diffusion modelling is based mainly on the reptation theory by de Gennes [
28,
29]. An important conclusion of this theory is that the penetration depth of chains through a plane in an entangled system is proportional to the fourth root of time,
. Wool et al. [
30,
31] have extended this theory to describe molecular diffusion through a polymer–polymer interface under isothermal conditions. For crack healing with instantaneous wetting, the diffusion coefficient
D is defined by Equation (1), where
σ is the healed interface strength,
σ∞ is the strength of the bulk material,
σ0 is the contribution to strength that is only created by intimate contact, and
K is a constant.
Jud et al. [
32] studied diffusion similarly and were also able to show that diffusion is proportional to
and that diffusion is faster at higher temperatures. They also observed that the diffusion coefficient
D can be described by the Arrhenius law. Considering these observations, Equation (1) can be reformulated as Equation (2), where
A is a constant,
EA is the activation energy, and
R is the universal gas constant.
Dara and Loos [
33] successfully used Equation (2) to describe the diffusion of the polysulfone, and Lee and Springer [
34] used it for PEEK 150.
Based on the previous models, Yang and Pitchumani [
35] have developed a non-isothermal model for the description of composite manufacturing processes. A temperature-dependent welding time
τw is used to describe the diffusion in Equation (3).
Yang and Pitchumani [
35] described
τw using the fitted Arrhenius equation of Lee and Springer [
34] to validate the model. Bastien and Gillespie [
36] have shown a similar approach using the Arrhenius law. For 3D printing, Li et al. [
37] applied the Arrhenius description to PLA (Polylactic Acid) and Yin et al. [
38] to ABS (Acrylonitrile Butadiene Styrene) and TPU (Thermoplastic polyurethane).
An alternative description of
τw, which has also been successfully applied to 3D printing, can be derived from rheological data as shown by Coogan and Kazmer [
27,
39] using HIPS (High Impact Polystyrene) or Bartolai et al. [
40] and Lepoivre et al. [
41] using ABS. Coogan and Kazmer [
27] additionally combined the diffusion model with a pressure-driven contact model to take neck growth into account in addition to diffusion and thus improve the accuracy of the prediction. Gilmer [
42] has compared the different approaches to
τw using the example of PEI (Polyetherimide) and shown that the various descriptions predict consistent trends for healing.
In the studies described so far, only amorphous thermoplastics have been investigated, whereby diffusion occurs as long as the interface temperature is above the glass transition temperature
Tg. With semi-crystalline thermoplastics such as PEEK, the bonding mechanisms are more complicated, as crystallinity build-up restricts neck growth and healing [
24].
To consider this influence, Barocio et al. [
43,
44] have coupled the diffusion model with the evolution of crystallinity. Diffusion is predicted using a fitted Arrhenius equation stopped after exceeding a critical crystallinity value of 5%. Good predictions for PPS (Polyphenylene sulfide) were made with this model. Consul et al. [
45] used a similar approach to compare the healing of PEEK and slow-crystallising PAEK (Polyaryletherketone). It was confirmed that the onset temperature of crystallisation significantly inhibits healing and can be seen as a critical threshold for the healing process. Basgul et al. [
46] used a diffusion model for PEEK based on rheological data. Assuming that the diffusion dynamics are negligible when crystallinity is formed, the diffusion was cancelled once the temperature fell below the melting point. Here, too, the experimental results support the model. In all of the modelling, mentioned above, of the healing process of semi-crystalline high-temperature thermoplastics, a contribution by intimate contact is neglected due to the high cooling rates.
The presented diffusion models are based primarily on the thermal history of the interface, which in turn is determined by the process parameters during 3D printing. Various methods are used to predict this thermal history. These range from 1D analytical models, such as those used by Thomas and Rodriguez [
47] or Sun et al. [
48], to 3D finite element models, such as those used by Zhang et al. [
49] or Zhou et al. [
50]. The modelling of the 3D-printed path is realised by element death and birth. Brenken et al. [
51] have shown that the simulation with the help of the FEM (Finite Element Method) can also be used to calculate the deformation and residual stresses during cooling.
To successfully apply the process of overprinting PEEK laminates to large structures, it is necessary to precisely understand and predict the bonding mechanism between laminate and 3D printing. To this end, this work will investigate to what extent the existing models for describing inter-layer bonding can be applied to in situ joining during overprinting. Firstly, the required material parameters are determined experimentally. The thermal history is then calculated using a 3D FEM heat transfer model. This information is then used in a healing model to calculate the bonding strength. The healing model is used to predict the effect of different process parameters on the bond strength. Both the heat transfer as well as the healing model are validated using experimental data from previous studies [
18,
19].
2. Materials and Methods
The structure of the study is shown in
Figure 1. To carry out the thermal analysis, the thermal properties of the 3D printing material are required, particularly the specific heat capacity
cp and the thermal conductivity
λ. The crystallisation temperature
Tc is particularly important for the healing model. These material data are first determined experimentally. In addition, experimental measurements of the bond strength
σexp and the interface temperature
Texp are required to validate the simulation models. The methodology and results of these measurements of
σexp and
Texp were described in previous studies [
18,
19]. With the help of all these measured values, a FEM analysis of the thermal history and, finally, the healing prediction are carried out.
2.1. Materials
The PEEK filament TECAFIL PEEK VX CF30 [
52] (Ensinger Plastics, Nufringen, Germany), filled with 30 wt % short carbon fibres, is considered for 3D printing. The high degree of carbon fibre filling increases the stiffness and reduces the thermal expansion of the printed component compared to pure PEEK. This reduces warpage during printing and also reduces the difference in stiffness between the printed component and the overprinted laminate, which is advantageous for the preceding mechanical tests.
The laminate, which is overprinted, consists of the UD (unidirectional), continuous fibre-reinforced tape Toray Cetex 1200 [
53] (Toray Advanced Composites, Morgan Hill, CA, USA) in the configuration [45/0/−45/90]
s. It is a PEEK tape with 66 wt % carbon fibres. The material properties of both materials are summarised in
Table 1. An example of a printed sample of short fibre-reinforced PEEK on the continuous fibre reinforced laminate is shown in
Figure 2.
2.2. Material Characterisation Methodology
2.2.1. Crystallisation Temperature Tc and Specific Heat Capacity cp
DSC (Differential scanning calorimetry) was performed using a DSC 214 Polyma (Erich NETZSCH GmbH & Co. Holding KG, Selb, Germany). The measurement was taken for three specimens (10 mg). The measurement program was run under a nitrogen atmosphere and with a heating and cooling rate of 10 °C/min. The samples were heated up and cooled down three times to 420 °C and 20 °C, respectively. The crystallisation temperature Tc was determined as the peak temperature of the crystallisation of the cooling curves. In addition, the melting peak temperature and glass transition mid-temperature were determined by the second and third heating curves.
The specific heat capacity
cp was determined using the same measurement setup. Sapphire was used as the reference material. The
cp curves were determined according to DIN EN ISO 11357-1 [
54].
2.2.2. Thermal Conductivity λ
The thermal conductivity was determined using LFA (Laser Flash Analysis). To produce the samples, 50 × 50 × 4 mm
3 plates were printed, from which round samples with a diameter of 12.6 mm and a thickness of 2.5 mm were then prepared. The LFA 457 MicroFlash measuring device (Erich NETZSCH GmbH & Co. Holding KG, Selb, Germany) was used to measure the thermal diffusivity
of the material. Pyroceram 9606 was used as the reference material. The measurements were carried out from 22 °C to 300 °C. The thermal conductivity
λ can be calculated from the thermal diffusivity by Equation (4)
where
a is the measured thermal diffusivity,
cp is the measured specific thermal capacity, and
ρ is the density.
ρ is assumed to be approximately constant at 1.38 g/cm
3.
2.3. Heat Transfer Model Methodology
The heat transfer model for calculating the thermal history of the interface between the 3D-printed component and the laminate was implemented using a FEM model in the software Ansys Mechanical (Ansys, Inc., Canonsburg, PA, USA), version 2023 R2. In the context of this work, the simulation results are to be evaluated using measured values from previous studies [
18,
19]. For this reason, the print setup for the mechanical test specimens was modelled in the simulation. The samples were initially printed with the GEWO HTP 260 (GEWO3D, Wörth, Germany) filament printer, which has a heated print bed and an enclosed, heated build chamber. The basic structure of the material deposition to be modelled is shown in
Figure 3.
In the model, the material deposition is modelled by element activation. The element activation is time-step-controlled by an Ansys APDL (Ansys Parametric Design Language) script. The print direction per layer can be freely selected. In this work, an infill with an orientation of ±45° is used as in the reference tests. In each time step, a new element is activated and the node temperatures of the element are set to the extrusion temperature for the duration of the time step. In the time step after depositing, the node temperatures are released, and the material can cool down according to the ambient conditions.
The investigated process parameters are represented by boundary conditions and convection loads. The nozzle or extrusion temperature is represented by the constraint of the newly activated element. The print bed temperature is also modelled by a boundary condition. For this purpose, the temperature of the underside of the laminate, which rests on the print bed, is limited to the print bed temperature. Convection cooling is applied to the free surfaces of the laminate and the already-printed material in accordance with the chamber temperature. The convection coefficient was calculated from the estimated flow conditions with a value of 300 W/(m
2 K). Finally, an additional convection load is applied under the nozzle to map the influence of the heated nozzle directly above the sample. The temperature of the convection load corresponds to the nozzle temperature as a simplifying assumption. The geometry of the simulated specimens is shown in
Figure 4a. The loads and boundary conditions are shown in
Figure 4b,c.
The element size was selected so that one element approximately covers the outlet surface of the nozzle. As a 0.4 mm nozzle was used for printing in this case, an element size of 0.4 × 0.4 mm
2 was selected. The maximum thickness of the elements is 0.4 mm. Since the layer thickness of the printed layer is thinner than 0.4 mm, the element thickness in the printed layers is the corresponding layer height. The layer heights are varied in this work, whereby the element thickness of the printed layers changes accordingly. The length of the time steps was selected so that the elements are activated according to the printing speed. This means that the nozzle is also applied to the model at the correct printing speed. With an element size of 0.4 mm and a printing speed of 12.5 mm/s, this means a time step of 0.032 s.
Figure 5a shows the meshed specimen during element activation, and
Figure 5b–e show a scheme of the element activation.
For the subsequent calculation of the bonding strength, the temperature profile in the interface between the printed material and the laminate is required. Evaluating a node directly in the interface between the newly activated element and the laminate does not make sense in this model, as these node temperatures inevitably correspond to the extrusion temperature due to fixing the node temperatures during deposition. A more sensible approach is to determine the temperature after a minimum penetration depth into the laminate to also consider the energy input into the laminate. For this purpose, a thin element plane with a thickness of 0.05 mm was inserted at the top of the laminate. As with all other elements, these are quadratic elements, and the interface temperature was evaluated at the centre node, i.e., at a distance of 0.025 mm from the surface. The setup for the temperature evaluation is shown in
Figure 6.
The density, specific heat capacity and thermal conductivity are required for the respective material model in the thermal simulation. While the density and heat capacity are direction-independent, the thermal conductivity of fibre-reinforced plastics is generally anisotropic. Material data are available in the literature for the PEEK UD tapes used to make the laminate. As suggested and successfully used by [
55], the data from [
56] were used in this work. The quasi-isotropic properties of the laminate were calculated from the data of the tapes according to the model of [
57]. The laminate is described by an in-plane and an out-of-plane value due to the quasi-isotropic fibre. The material properties of the laminate used are summarised in
Table 2. The material parameters required to describe the short-fibre-reinforced PEEK-CF 3D printing material are determined experimentally as part of this work. A slight anisotropy is also to be expected for 3D printing material. However, since only the first layer is relevant in this model and the thermal conductivity perpendicular to the printing direction is dominant for the heat input into the interface, the model is simplified and assumed to be an isotropic material with the thermal conductivity perpendicular to the printing direction.
Using this model, a total of 15 parameter variations were calculated, whereby the nozzle temperature, the print bed temperature, the build chamber temperature and the layer thickness of the first layer were varied. The build chamber temperature is always 10 degrees below the print bed temperature. All other process parameters were kept constant. Previous analysis has shown that the extruded material’s melt temperature in the given range is approximately 54.6 °C below the set nozzle temperature. This difference was taken into account accordingly in the simulation. The parameter ranges are summarised in
Table 3. A detailed list of all parameters can be found in
Table A1 in
Appendix A.
2.4. Healing Model Methodology
As already described, the layer bonding in 3D printing is primarily driven by intimate contact, neck growth and diffusion. Similar behaviour is expected in the bond between the printed material and the laminate during overprinting, as the same thermoplastic is present as a matrix in both the laminate and the 3D printing filament. Various investigations also suggest that the
σ0 component due to intimate contact, as suggested by Wool et al. in Equation (2), is negligible [
40,
41,
44,
45,
46,
58,
59,
60]. This agrees with the observations of the previous experiments on overprinting [
18,
19], in which pure wetting does not lead to any measurable bond strength.
Assuming that the bonding is mainly caused by diffusion, the non-isothermal healing model presented by Yang and Pitchumani [
35], as in Equation (3), is used to predict the strength between the 3D-printed material and the laminate. The fitted Arrhenius equation by Lee and Springer [
34] is used to describe
τw. This model was adapted for PEEK 150, which is also used for 3D printing in this study. In addition, Yang and Pitchumani [
35] have already successfully tested the model in their own work.
One difference between traditional 3D printing and the overprinting of laminates is that in the case of overprinting, the temperature of the substrate cannot be influenced by the print settings. Accordingly, the thermoplastic in the laminate is already crystallised, and the energy input to enable bonding in the interface must take place entirely through the newly printed layer. Assuming that diffusion mainly occurs in the amorphous state and is so strongly inhibited by crystallisation that a contribution in the crystalline state is negligible, this means that the interface temperature must be brought above the melting temperature of PEEK during overprinting. In addition, diffusion only occurs in the time interval between the deposition time
td and the time of crystallisation time
tc during the cooling phase. This time interval is shown schematically in
Figure 7.
Taking into account the assumptions for
τw and the time interval for diffusion, Equation (3) results in Equation (5), which is used below to calculate the strength between 3D printing and laminate. As no fibres can run through the interface layer between the laminate and 3D print, the fully healed bond strength
σ∞ is assumed to be the strength of the used PEEK matrix. The average strength of printed PEEK is specified by the manufacturer as 90 MPa [
61]. Therefore,
σ∞ is assumed to be 90 MPa for this work.
Using Equation (5) and the temperature curve from the thermal calculation, the bond strength is calculated for all parameter variations in
Table A1 in
Appendix A. The prediction method is evaluated by comparing these calculated strengths with the measured values.
2.5. Statistics
To compare the simulation results with the experimental values, the results were integrated into the statistical evaluation of the experiments. The assessment was carried out in the DoE software Design Expert, version 23.1.5 (Stat-Ease, Inc., Minneapolis, MN, USA). Surface response models were created with this software using the simulation results and compared with the models of the experimental values. The 95% confidence interval was specified for all models. In addition, statistical correlations between the experiment and simulation were determined and tested for significance using ANOVA (analysis of variance). The correlations are indicated by the Pearson correlation factor r. Correlations with a p-value below 0.05 are considered significant.
4. Discussion
The characteristic properties of the interface’s temperature curves could be mapped well in the transient thermal heat transfer calculation. The influence of the toolpath planning, the moving hot nozzle, and the material discharge behaved as in the measurements. The cooling behaviour is also qualitatively consistent. Accordingly, the effects of the process parameters on the important parameters were also reproduced in qualitative agreement with the test results.
Overall, however, both the maximum temperatures and the cooling rates were predicted to be higher than those measured in the test. This can be seen in the effect plots shown, but also in the direct comparison of the temperature curves as in
Figure 11. A very good agreement can be found in the literature for simple single-wall geometries. Sun et al. [
48] compared various analytical models and achieved good results. Lepoivre et al. [
41] were able to map the temperature curve of single-wall geometries very accurately in the multiphysics software COMSOL. However, with more complex 3D models, deviations often occur as in this work. The FEM model by Yin et al. [
38] also predicted significantly higher temperature peaks than measured. Basgul et al. [
46] were able to show that these deviations can shift over several layers.
One possible cause of deviation in this work may be the type of temperature measurement used in the experiment. Type K thermocouples with a diameter of 0.25 mm were used. The response time of these thermocouples is very short but can still have a small influence. The embedding of the elements in the laminate is more decisive. In the simulation, the measuring point is 0.025 mm below the surface, and there is a perfect heat transfer to the temperature evaluation node. In the measurement, the thickness of the matrix layer on the thermocouple can vary slightly. The heat transfer from the matrix to the thermocouple is probably not ideal, either. In addition, the heat transfer in the vertical direction between the 3D print and the laminate is also ideal in the simulation. In reality, porosity can occur here, and incomplete wetting further impairs heat transfer, which presumably results in poorer heat transfer in the vertical direction compared to the horizontal direction. In the measurements [
19], a porosity of 15–20% was found in the 3D-printed material. In the boundary layer, the porosity is significantly lower, but the exact influence is not known at the time of this work.
Another cause may lie in the loads and boundary conditions of the simulation. The heat transfer coefficient of the convection conditions was calculated from the estimated flow conditions. The heat transfer from the 3D-printed layer to the laminate is also not exactly known. Certain deviations may occur here, especially with regard to the cooling rates.
For a final validation of the heat transfer model, a more detailed campaign is necessary. In particular, the sources of error from the measurement campaign, especially the embedding of the thermocouple and the heat transfer from the laminate to the thermocouple, must be better characterised. In addition, a simpler geometry, e.g., single-wall geometries, should be selected for these tests to avoid superimposed effects from rapid tool movements above the measuring point. In addition, the limiting heat transfer between printed boundary layers should be investigated in more detail.
The healing model initially predicted the effects of the process parameters only inadequately. The results showed that the interface temperature curve was insufficient to simulate the bonding mechanisms when overprinting the laminates in the experimental study. Lee and Springer [
34], as well as Yang and Pitchumani [
35], came to good agreement with their experiments using the same approach for the welding time
τw for PEEK. However, both studies used a manufacturing process with considerable consolidation pressure, which presumably makes the influence of wetting negligible. With 3D printing, a few authors, such as Li et al. [
37], have successfully predicted the strength with reasonable accuracy without considering the actual wetted area. However, these are also thermoplastics that exhibit good wetting behaviour, especially PLA. Other authors consider the wetting effects intrinsically when the model is fitted by experiments in the same process, as seen in Barocio et al. [
44] or Yin et al. [
38].
In this work, a linear coefficient was introduced that considers the ratio of the ideal wetted area to the actual wetted area in the model to improve the prediction. A similar approach was used by Consul et al. [
45] for PEEK, where the factor mainly takes porosity into account. Coogan and Kazmer [
27] have shown that the consolidation pressure due to extrusion significantly influences the actual wetted area and have described this using a wetting factor. This approach has led to very good results. As this consolidation pressure is primarily influenced in this work by the fluctuations in the layer height and the associated over- or underextrusion, the approach seems suitable for describing the effects.
The measured strengths from the experimental study are subject to a high degree of scatter, making final validation of the healing model difficult. In addition, the scatter is projected onto the simulated strengths using measured values for the wetting coefficient. The measurement of the layer thicknesses is also subject to a certain degree of measurement inaccuracy, which is not precisely known here. Overall, the calculated strengths are lower than the measured strengths. This may be because the welding time τw model is not optimised for the specific material, but it may also be an effect of the high cooling rates from the heat transfer model. Some factors are also not taken into account in the model. According to the manufacturer, the tapes used in the laminate should have a matrix-rich surface, but there can still be contact between the fibre and the 3D printing material, which is not modelled. Likewise, the influence of the short fibres and the porosity in the 3D printing material is not considered.
To improve the model, a separate campaign to fit
τw should be carried out in future studies. At the same time, the influence of process inaccuracies should be reduced. The precision with which the first layer height can be set depends heavily on the printer used. By using a newer-generation printer, the scatter can probably be greatly reduced. In addition, the exact nature of the interface must be better determined. This includes both the proportion of fibres and the proportion of porosity. A contact model such as that developed by Coogan and Kazmer [
27] can make a useful contribution.
Nevertheless, important conclusions for process development can be derived from the results. In particular, the accuracy of the first layer is a critical factor when large laminates are to be printed with robot-based printers. The positioning accuracy of the robots is often in the same order of magnitude as the layer height. Accordingly, it will be necessary to use very precise, highly calibrated robots. Likewise, the tolerances of large laminates are often greater than the layer thickness. Therefore, it will be necessary to capture the real geometry very precisely and carry out the path planning on this real geometry. These findings are consistent with the experimental results of Atzler et al. [
15].