1. Introduction
Continuous carbon fiber reinforced polymer (CFRP) composite materials exhibit excellent specific strength and stiffness properties [
1,
2]. Nowadays, composite materials are extensively employed in various spacecraft, including the A380. In the aerospace industry, wall panel structures are widely used as essential load-bearing components. Utilizing composite materials for the construction of these panels has led to significant weight reduction [
3]. The flight efficiency of the aircraft has increased. Composite wall panel structures are generally made up of variable thicknesses of skins, stiffeners, honeycomb or foam filling materials, etc., have complex cross-sections, and are large-scale. Autoclave process technology is a commonly used method for manufacturing composite materials. During the composite curing process in an autoclave, curing distortion is a common phenomenon in composite wall structures. This distortion not only affects the mechanical properties of the wall panel structure [
4] but also hinders the assembly of components [
1]. Hence, effectively mitigating the distortion of large-scale and complex cross-section composites has become a focal point and a challenging area of research [
5].
Currently, the primary methods for mitigating distortion during the manufacturing of composites in an autoclave include the traditional trial-and-error method [
6], the optimized design process parameters method [
7,
8,
9,
10,
11,
12], the mold profile compensation method [
13,
14,
15,
16,
17], the hot sizing process method [
18,
19], and other control methods [
20]. The traditional approach relies on experience and a trial-and-error process. It involves repeated adjustments and compensations of curing process specifications and mold profiles to control the degree of distortion. However, the use of traditional trial-and-error methods significantly increases costs for the production of composite wall panel structures. Despite the cost implications, this traditional method is still widely employed for large-scale composite components manufactured across various companies.
Thanks to the rapid advancements in finite element technology, we now have favorable conditions for delving deeply into solving the problem of distortion in composite structural parts, particularly in optimizing process parameters. Ren et al. [
21] have studied the 3D woven composite process, developing process analysis agent models and optimizing process parameters. Their results demonstrate a reduction in residual strain and process cycle time with the use of optimized parameters. Manjusha et al. [
22] have employed FBG sensors to monitor the curing process for changes in fiber volume within the resin matrix and composite material. Based on monitoring results, they have optimized the curing process parameters. Their findings reveal a reduction in residual stresses, process costs, and process cycle times within the interior of the composite component.
Nele et al. [
23] conducted a study on the hot press molding process of thermoset resin matrix composites. They found that the two primary factors influencing laminate thickness, fiber percentage, and pore volume are external pressure and the timing of pressurization. Optimizing the timing of pressurization was effective in achieving the objective of reducing process costs and cycle times. However, when using the process parameters optimization method, a challenge arose in efficiently mitigating induced distortion for large-size and complex composite structures. In the literature [
3,
4,
24,
25,
26,
27], various approaches have been explored to predict and control distortion in composite components. Modifying the manufacturing mold profile is one method employed to manage component distortion. Despite extensive research, achieving perfect accuracy in predicting distortion, especially in large-scale and structurally complex cross-section composite components, remains challenging. Inaccurate distortion predictions can lead to time-consuming and costly redesign and rework of composite moldings [
26]. Additionally, the maximum compensation amount significantly influences the accuracy of mold profile compensation, which, in turn, impacts the forming accuracy of the parts.
In the literature [
18,
19], the hot sizing process is described as a method in which a component is placed onto a mold that conforms to its shape under an external load, heated to a high temperature for a specific duration, and then unloaded to correct the profile of the composite material component. Liu et al. [
24] investigated the fundamental principles of the hot sizing process for composite materials and conducted experimental studies on small composite structural components. The hot sizing process can partially modify the shape of composite components. However, it requires the design of specialized tooling, increases manufacturing costs, and has a detrimental effect on the strength and stiffness of the composite component.
In summary, the existing methods for mitigating curing distortion have limitations when applied to large-scale and complex cross-section composite structures. These limitations stem from the reliance on prediction accuracy, the associated high manufacturing costs, and the less-than-ideal effectiveness of distortion control. Therefore, we investigate the limitations of previously discussed control methods and present a refined approach to manufacturing composite parts.
This paper presents a global compensation method designed for large-scale and complex cross-section composite structures, addressing the challenge of distortion control in the autoclave process of composite wall panel structures. The approach involves establishing a coordinated model that links the refinement of design curing process parameters and the mold profile compensation method. A coordinated model simulation approach has been developed for large-scale, complex cross-section composite wall panel structures, predicting the final geometry of the wall panel structure. The study investigates the influence of heating, holding, and cooling times on distortion. To validate the method’s effectiveness, full-scale curing experiments were conducted using the autoclave process with a large-scale, complex cross-section composite wall structure measuring 1700 mm × 2000 mm. The refined manufacturing process achieves high-quality results for large-scale and complex cross-section main load-bearing composite structures, offering a theoretical foundation and practical value for the application of composites in the aerospace industry.
2. The Global Compensation Method and Coordinated Model
Due to irreversible curing distortion upon demolding, which fails to meet engineering’s practical requirements [
28,
29], existing methods struggle to effectively suppress distortion in thermoset composites processed in autoclave, especially for large-scale complex cross-section components. Achieving high-precision modeling with these methods remains challenging. Recognizing the limitations of current distortion control methods, this paper introduces a collaborative approach based on the global compensation of composite structural components. Central to this approach is the acquisition of the global compensation amount. The following section outlines the modeling process for the control method and the procedure for obtaining the global compensation quantity, known as the collaborative model.
First, we design the optimal curing process parameters to mitigate the curing distortion of the composite component while adhering to cost constraints. Next, we establish coordinated models, as illustrated in
Figure 1a,b. These models consist of the theoretical design model’s inner surface and the outer profile of the component after curing and distortion. On the theoretical profile, we select ‘n’ nodes, denoted as
ni (
i = 1~
n). Since the grid comprises four-node elements, each element’s area is represented by the element weight ratio
Si. For every four-node tetrahedral mesh element (or hexahedral mesh element), we set a projection distance along the normal direction, denoted as
hj (
j = 1~
n), from point 1 to point 2.
We assume that there are ‘
m’ grids on the surface of the simulation component model. The model for calculating the weighted average of cured distortion in the simulated composite component model is represented by the following:
where
Si stands for the area of the
i-th grid on the surface of the simulation component model, and
hj represents the distance from the
j-th node on the grid of the simulation component model to the manufacturing profile of the theoretical mold model along the normal direction.
The model for calculating the root mean square distortion value in the simulated composite component model is as follows:
where
hj denotes the distance from the
j-th node on the grid of the simulation component model to the manufacturing profile of the theoretical mold model along the normal direction.
We obtain the mean value of weighted distortion, the root mean square distortion, the minimum distortion value, and the maximum distortion for group k. To select the smaller value for global compensation, we follow this method: first, we arrange the weighted distortion averages into k groups, from smallest to largest. Then, we select the first k/2 + 1 groups of weighted distortion averages and find their corresponding root mean square distortion values. Next, we arrange the k/2 + 1 sets of root mean square distortion values obtained in the first step from smallest to largest and choose the front k/4 + 1 groups, finding their corresponding minimum distortion values. We then organize the k/4 + 1 groups of minimum distortion values obtained in the second step from smallest to largest, select the front k/8 + 1 groups, and find the corresponding maximum distortion values. Finally, we arrange the k/8 + 1 groups of maximum distortion values from largest to smallest and select the very smallest of the distortion maxima as the smaller value for global compensation.
The process of obtaining the optimal compensation profile and mold compensation is depicted in
Figure 2. Firstly, we conduct a refined design of the curing process parameters, as shown in
Figure 2a. Based on the curing process parameters and their adjustable ranges provided by the supplier, multiple combinations of process parameters (k1, k2, k3, …, kn) were designed using the Design of Experiments (DoE) method. Utilizing PAM-Distortion (2014) software, simulation analyses were conducted to obtain the curing deformation values (D1, D2, D3, …, Dn) corresponding to different combinations of process parameters. In the simulation analysis, the curing deformation values (D1, D2, D3, …, Dn) were obtained for the respective combinations of process parameters (k1, k2, k3, …, kn). Subsequently,
Dav and
Dmsr were calculated using Formulas (1) and (2). A four step process of ranking and selection was performed to ultimately obtain a set of process parameters and their corresponding cured component distortion results, as shown in
Figure 2b. The obtained cured component deformation results serve as the optimal mold compensation profile. Finally, the optimal compensation profile and the mold surface to be compensated for are imported into the software, and the mold surface is compensated for based on the traditional nodal reverse compensation algorithm. The compensated mold surface is then outputted, and the compensation effect is compared and analyzed using both finite element methods and curing experiments for verification, as shown in
Figure 2c.
This marks the completion of the coordinated model. Finally, the smaller value for the global compensation of the mesh surface of the simulated component model corresponds to the manufacturing mold profile obtained using compensated finite element (2014) software.
3. Materials, Systems, and Properties
The prepreg material system for braiding consists of T800 carbon fiber and 603A epoxy resin [
30]. Each single layer of prepreg has a thickness of 0.2 mm, and it achieves a fiber volume rate of 56%. For filling materials, we use Polymethacrylimide (PMI) foam with a density of 110 kg/m
3 and an elastic modulus and strength of 135 MPa and 2.2 MPa, respectively. Additionally, we employ ortho-hexagonal Nomex paper honeycomb structures with a density of 32 kg/m
3 and equivalent elastic modulus and strength values of 623 MPa and 60 MPa, respectively. The composites are cured at 165 °C, with a heating time of 5.6 h, a holding time of 4 h, and a cooling time of 6.25 h, resulting in an initial total curing time of 15.85 h. The curing process is carried out under a pressure of 0.3 MPa. For thermo-chemical parameters and fundamental mechanical properties of the T800 carbon fiber/epoxy composite, please refer to
Table 1 and
Table 2, respectively.
ρc represents the composite material density, which can be calculated as a weighted average of volumetric content from the density of resin and fibers, indicated with the symbols ρm and ρf, respectively; Cp,c. denotes the composite-material-specific heat, which can be determined as a weighted average of weight content from the specific heat of fibers and resin. The thermal conductivity of a single unidirectional ply can be defined by two terms: the conductivity along fibers, Kl, and the perpendicular conductivity, Kt. The resin total reaction heat is Hr, E represents the activation energy, A the frequency factor, and m and n the reaction orders. λ is a parameter characteristic, Tg∞ is the maximum glass transition temperature, and Tg0 the minimum temperature.
3.1. Curing Kinetics Model
The curing kinetics model illustrates the quantitative relationship between the resin’s cure rate, the degree of cure, and the temperature. We conducted five sets of DSC experiments with varying rates of warming. These experiments used heating rates of 2, 5, 10, 15, and 20 °C/min, with each group repeated once.
Figure 3 presents the results of the dynamic DSC scan tests at different ramp rates. As the temperature increase rate escalates, the curing reaction rate of the 603A resin decreases, and the time required to reach peak heat flow increases.
The starting temperature (
Ti), peak temperature (
Tp), termination temperature (
Tf), and the total amount of heat released after the complete reaction (
Hu) for the curing reaction of 603A resin at different temperature rise rates (
β) are presented in
Table 3. The average total heat release after the complete curing reaction of 603A resin is 403.5 kJ/kg.
Based on the characteristic temperature of the exothermic peak of the DSC curve at different ramp rates, the
T-
β extrapolation method was used to determine the curing process temperature of 603A resin, as shown in
Figure 4. The curing process temperatures for 603A resin include 151.3 °C for gelation, 193.9 °C for curing, and 253.6 °C for post-treatment. In the actual curing and molding process, other factors must be taken into consideration when determining the curing temperature for the component. For instance, when the skin is co-cured with the frame beam as a whole, including a sandwich layer, this can reduce the required curing temperature and extend the holding time.
In summary, the kinetics of 603A epoxy resin curing are modeled by the following equation:
where
R represents the universal gas constant,
α the cure degree, and
T the temperature.
3.2. Heat Transfer Model
In an autoclave, air is heated to control the temperature of the mold and the component during the curing process through solid heat transfer. The temperature transfer and distribution within composite components are regarded as a nonlinear endothermic problem. This is based on Fourier’s law of heat transfer and the law of conservation of energy, leading to the establishment of the following equation as the governing equation for heat transfer and distribution in an autoclave [
31,
32,
33]:
where
T stands for temperature,
CT represents the specific heat of the material, and
kx,
ky, and
kz are the coefficients of heat transfer along the
x,
y, and
z directions.
is the rate of heat generation related to the exothermic nature of the curing reaction and is expressed as the following equation [
34]:
where
t is time,
Vf is the fiber volume content,
Hr is the total exothermic reaction heat per unit mass of resin cured, and
α is the degree of cure.
3.3. Stress–Strain Constitutive Models
Thermoset composites undergo curing reactions during the molding process, with the degree of cure of the resin increasing with temperature and time. The phase state transitions through three stages: viscous flow state, rubbery state, and glassy state [
35,
36], leading to significant changes in mechanical properties, as depicted in
Figure 5.