Figure 9 - uploaded by Guiwei Dong
Content may be subject to copyright.
Schematic diagram of the formation processes of the unfoamed skin layer in microcellular injection molded part: (a) during the filling stage; (b) after the filing stage. 

Schematic diagram of the formation processes of the unfoamed skin layer in microcellular injection molded part: (a) during the filling stage; (b) after the filing stage. 

Source publication
Article
Full-text available
The microcellular injection-molded part usually consists of a foamed core region and two unfoamed skin layers on the cross section. This paper investigated the formation process, formation mechanism and structural characteristics of the unfoamed skin layers in microcellular injection-molded part. It is found that the unfoamed skin layers are formed...

Context in source publication

Context 1
... of the flow front, the cells on both sides of the cross section are deformed and stretched further, the structure of the skin region is becoming more and more compact. In the tail position of 20 mm away from the flow front, as shown in Figure 6(6), the deformed cells in the skin region almost disappear, a compact solid-like skin layer is formed. The formation mechanism of this kind of unfoamed skin layer will be analyzed in the following section. Through analyzing the morphologies of the unfoamed skin layers in microcellular injection-molded parts with different shot sizes, we can find that the structural morphology is different at different locations of a same microcellular injection- molded part. Generally speaking, the unfoamed skin layer in microcellular injection molded part has two kinds of morphologies: one is that the unfoamed skin layer and foamed core region have a transition region and without obvious boundaries between them, the other is that the unfoamed skin layer and foamed core region have no transition region and with obvious boundaries between them. Obviously, the formation process and formation mechanism of these two kinds of unfoamed skin layers are different and also complex, it cannot be easily explained by just the cooling solidification behavior of the polymer-gas solution. In our previous studies, we have found that there are two cell forming processes, ‘‘foam during filling’’ process and ‘‘foam after filling’’ process, in microcellular injection-molding process, and the melt pressure in the filling stage is the dominant factor affecting the cell forming processes. In filling stage, the melt near the flow front with a pressure lower than a critical pressure value will foam during filling. But the melt near the gate with a pressure higher than the critical pressure value will not foam during filling, and it foams in cooling stage after filling stage. 27 These two kinds of cell forming processes in microcellular injection molding are shown in Figure 7. Also, we know that the molten polymer melt is a typical non-Newtonian fluid and renders typical viscoelastic behavior. In the filling stage, the polymer melt filling flow is a type of laminar shear flow and exhibits fountain flow at the flow front. Figure 8 schematically gives the melt filling flow behaviors in the filling stage. From this figure, we can find the melt flow velocity is smaller at the mold wall but higher at the center of the mold cavity, which results in a large shear rate gradient. Figure 8 also shows the fountain flow effect at the flow front. This effect forces the melt at the flow front lay down a skin layer towards the two mold cavity surfaces and the melt at the center of flow front flows forward and fills the mold cavity. Meanwhile, for most of the injection molding processes, the temperature of mold is much lower than that of the polymer melt, so when the skin melt contact with the mold, it will cool down quickly and form a thin frozen layer. From the above analyses, it is known that in microcellular injection molding process, the melt with pressure lower than the critical pressure foams during the filling stage. And the region of this foamed melt during filling stage is from the flow front to the position where the critical pressure lies. Opportunely, this region just corresponds to the place where the laminar shear flow behavior of the polymer melt and fountain flow behavior of the flow front are all relatively severe. So the melt filling flow behaviors will have a significant effect on the structure of cells formed in the foaming process during filling. The bubbles or cells formed in ‘‘foam during filling’’ process will be deformed by the shear stress of the laminar flow field. As the shear rate gradient shown in Figure 8, the bubbles in the center layer will have a near-spherical shape due to a zero shear rate at this region. But since the shear rate becomes large gradually from the center to the cavity wall, the bubbles’ shape will be deformed more and more severely from a near sphere to a spindly ellipsoid. 28 At the same time, the filling flow behavior of the melt at the flow front is not laminar flow but a fountain flow behavior. The deformed bubbles will be continu- ously pushed from the center layer out to the skin layer and finally to the surface. As the flow front moves forward, the bubbles’ shape will be deformed more and more severely, changed into long and thin strips or eventually broken down into a series of smaller bubbles under the large shear rate and extrusion forces. For the polymer melt with a pressure higher than the critical pressure value, it will not foam during filling, so the melt filling flow behaviors have a small effect on it. Because the melt filling flow behaviors have different effects on the two cell-forming processes, here we also divide the formation of the unfoamed skin layer in microcellular injection molding into two processes: ‘‘during filling’’ and ‘‘after filling’’. Figure 9 gives the two forming processes of the unfoamed skin layer ‘‘during filling’’ and ‘‘after filling’’. In ‘‘during filling’’ process, as shown in Figure 9(a), the melt near the flow front generates ‘‘foam during filling’’ process, the laminar shear flow of the melt causes the formed cells deforming and the fountain flow at the flow front push the deformed cells out to the cavity walls. Once the deformed cells in frozen layer region contact the cold mold walls, they will be frozen quickly and retained in the frozen layer. While for the deformed cells outside the frozen layer region, as the flow front move forward, the cells are deformed further into thinner and longer cells by the shear flow of the melt. Meanwhile, the pressure of the melt at this position increases gradually and the contact surfaces between the cells and polymer melt increase too due to further deformation of the cells. Under a certain pressure, these severely deformed cells will re-dissolve into the polymer melt to form a solid-like compact skin layer. This is the formation process and formation mechanism of the unfoamed skin layer in ‘‘during filling’’ process. In ‘‘after filling’’ process, as shown in Figure 9(b), the melt near the gate begins to foam. At this moment, the melt is beginning to cool and solidify, and the temperature of the melt near the mold walls decreases quickly. Therefore, only the melt in the core region has a relatively high temperature and can foam. The melt near the mold cavity walls has a relatively low temperature and will not foam, and finally form an unfoamed skin layer. This is the formation process and formation mechanism of the unfoamed skin layer in ‘‘after filling’’ process. Once the unfoamed skin layer is formed in ‘‘during filling’’ process, its viscosity is much different from that of the cell and polymer mixture which continue to move through the centre. This difference in viscosity makes their flow velocities have obvious difference and form a clear boundary between them. For the unfoamed skin layer formed in ‘‘after filling’’ process, it is formed in cooling stage. Since the transition of temperature field on the cross section is relatively smooth, the boundary between the formed skin layer and the foamed core region is not observed obviously. The closer to the core region the melt is, the higher the temperature of the melt is, the smaller the foaming resistance is and finally the bigger the cell size and the cell density are. On the contrary, the closer to the skin layer the melt is, the lower the temperature of the melt is, the bigger the foaming resistance is and finally the smaller the cell size and the cell density are. Furthermore, if the temperature of the unfoamed skin layer formed in ‘‘during filling’’ process is relatively high enough, it may generate the second foaming process, and a small number of cells are formed in the skin layer near the foamed core region. But these newly formed cells are small both in cell size and cell density due to the overall low temperature in this moment. According to the above analysis on the formation process and formation mechanism of the unfoamed skin layer, it is known that the unfoamed skin layer in microcellular injection-molded part consists of two regions, the outer region is a thin frozen layer that has deformed and broken cells inside, and the inner region is a relatively compact solid-like layer that has no visible cells inside. Figure 10 shows the SEM pictures of the unfoamed skin layer in microcellular injection-molded part and the amplified views of the frozen layer. It can be seen that the structural characteristics of the unfoamed skin layer is not identical, the outer frozen layer region is relatively loose. From the amplified views of this thin loose layer, it can be seen that there are a number of deformed cells. When the melt contacts the cold mold walls in filling stage, it is frozen quickly, the deformed cells are solidified and their morphologies remained directly. Therefore, this loose layer is the frozen layer formed very quickly in melt filling process. Besides, from the amplified views of the frozen layer, it can also be seen that there are rough and clutter cells on the surface of the microcellular injection-molded part. This is because in the filling stage, the cells on the flow front were broken and pushed out by the fountain flow behavior. When they contact with the cold mold wall, they freeze quickly, the gas has no time to escape and retains on the part surface. This is also the primary reason that the flow marks usually exist on the surface of microcellular injection-molded parts, as shown in Figure 11. Since the inner region of the unfoamed skin layer in microcellular injection- molded part has no visible cells, it looks like the solid part molded by the conventional injection molding. However, they are different in nature. The essential difference is that there is dissolved gas in the unfoamed skin layer. Figure ...

Similar publications

Article
Full-text available
The material-inherent specific volume behavior of polymers is highly important for producing dimensionally accurate injection molded parts since the shrinkage and the shrinkage-induced warpage are attributable to the specific volume behavior. Thereby, the prevalent process parameters melt temperature and cavity pressure significantly influence the...
Article
Full-text available
Abstract: Thermoplastic matrix polymer composites have gained commercial success in the semi structural and structural applications. Polyethylene (PE) is one of the most versatile and widely used thermoplastics in the world because of its excellent properties like toughness, near-zero moisture absorption, excellent chemical inertness, low coefficie...
Conference Paper
Full-text available
The substitution of conventional materials using technical plastic materials offers a high potential for integration of functions into plastics products. In this context, the light-weight design aspect as well as the simplification of complex production processes can be addressed. As an example, plastics can be modified to transfer an electrical ch...
Article
Full-text available
Injection molding is in high demand in several industries due to its efficiency and versatility. Quality control plays a crucial role in ensuring the excellence of plastic products during injection molding. However, the phenomenon of weld lines has persisted due to the susceptibility of melt flow in the mold cavity for independent or multiple relat...
Article
Full-text available
The cavity pressure in the injection molding process is closely related to the quality of the molded products, and is used for process monitoring and control, to upgrade the quality of the molded products. The experimental platform was built to carry out the cavity pressure experiment with a micro spline injection mold in the paper. The process par...

Citations

... As cell growth and cell nucleation are competing mechanisms, and CD drops in the core layer and increases in the shell regions [3,[44][45][46]. All samples showed a solid skin layer, which is caused by the rapid solidification of the melt [47,48]. Similar to fiber microstructure, CD and CS distributions impact the mechanical response of foamed components [49]. ...
Article
Full-text available
To maximize the driving range and minimize the associated energy needs and, thus, the number of batteries of electric vehicles, OEMs have adopted lightweight materials, such as long fiber-reinforced thermoplastics, and new processes, such as microcellular injection molding. These components must withstand specific loading conditions that occur during normal operation. Their mechanical response depends on the fiber and foam microstructures, which in turn are defined by the fabrication process. In this work, long fiber thermoplastic door panels were manufactured using the Ku-FizzTM microcellular injection molding process and were tested for their impact resistance, dynamic properties, and vibration response. Material constants were compared to the properties of unfoamed door panels. The changes in mechanical behavior were explained through the underlying differences in their respective microstructures. The specific storage modulus and specific elastic modulus of foamed components were within 10% of their unfoamed counterparts, while specific absorbed energy was 33% higher for the foamed panel by maintaining the panel’s mass/weight.
... Typical supercritical fluid (SCF) foaming agents such as N 2 and CO 2 have a critical pressure of 34 bar and 71 bar, respectively [109]. The melt pressure lower than the critical pressure of SCF induces cell formation at the flow front region in the filling stage as shown in Fig. 15a [110]. The cells are oriented and stretched by the shear deformation in the flow direction and the elongational stress at the flow front, respectively [30,35]. ...
... Therefore, the surface material easily replicates microscale structures of the mold surface or fills the small gaps between reinforcing Fig. 15. Underlying mechanism of the bubble marks on the foam injection-molded surface, (a) during the filling stage, (b) after the filling stage [110]. (Reproduced with permission). ...
Article
Full-text available
Injection molding is an efficient manufacturing process for mass-producing parts with complicated geometry, consistent quality, and attractive appearance. With the increasing dependency of consumers’ decisions on the aesthetic and design attraction of the products, improvement of surface quality has been one of the main areas for research and development of injection molding technologies. This paper presents a comprehensive overview of injection molding for high surface quality based on the optical aspect of surface quality and defects. It classifies the recent research and development into four sections, namely, measurement, influencing factors and causes, prediction, and control of surface quality and defects. Based on those reviewed studies, this paper proposes further research and development topics for high surface quality injection-molded products.
... Foaming also plays a significant role in the packing stage, resulting in shrinkage reduction, warpage minimization, and the elimination of residual stresses, etc. Studies on the process characteristics of MuCell ® and the associated molded-part properties have been reported earlier [4][5][6][7][8][9][10][11][12][13][14][15][16][17][18][19][20][21]. ...
Article
Full-text available
Microcellular injection molding technology (MuCell®) using supercritical fluid (SCF) as a foaming agent offers many advantages, such as material and energy savings, low cycle time, cost-effectiveness, and the dimensional stability of products. MuCell® has attracted great attention for applications in the automotive, packaging, sporting goods, and electrical parts industries. In view of the environmental issues, the shoe industry, particularly for midsole parts, is also seriously considering using physical foaming to replace the chemical foaming process. MuCell® is thus becoming one potential processing candidate. Thermoplastic polyurethane (TPU) is a common material for molding the outsole of shoes because of its outstanding properties such as hardness, abrasion resistance, and elasticity. Although many shoe manufacturers have tried applying Mucell® processes to TPU midsoles, the main problem remaining to be overcome is the non-uniformity of the foaming cell size in the molded midsole. In this study, the MuCell® process combined with gas counter pressure (GCP) technology and dynamic mold temperature control (DMTC) were carried out for TPU molding. The influence of various molding parameters including SCF dosage, injection speed, mold temperature, gas counter pressure, and gas holding time on the foaming cell size and the associated size distribution under a target weight reduction of 60% were investigated in detail. Compared with the conventional MuCell® process, the implementation of GCP technology or DMTC led to significant improvement in foaming cell size reduction and size uniformity. Further improvement could be achieved by the simultaneous combination of GCP with DMT, and the resulting cell density was about fifty times higher. The successful possibility for the microcellular injection molding of TPU shoe midsoles is greatly enhanced.
... Microcellular Injection Molding (MIM) is a less widespread technology, having recently emerged as an alternative to conventional methods, supported by the lightweight trend, in order to reduce the consumption of raw material needed to produce a finished component [14e16]. With this type of injection molding technology, the molded components are produced with a cellular structure, typically the cells have micro dimensions, 1e100 mm, and a density of 10 7 e10 15 cell/cm 3 , providing weight reduction (5%e 30%) driven by the hollow core of comprising cells [8,17,18]. The typical cellular structure resulting from MIM technology can be obtained by the introduction of blowing agents in the melted polymer during the injection molding process, creating a onephase solution during plasticization [19,20], through controlled conditions of pressure and temperature [21]. ...
Article
Full-text available
Microcellular Injection Molding (MIM) is a variant of injection molding technology used to manufacture plastic components, with a cellular structure and reduced weight. However, this technology is characterized for producing components with a poor surface finish and impacted structural integrity. To improve the molded surface appearance, the MIM process conditions have been thoroughly studied, nevertheless, some marks are often noticeable. For this reason, the combination of MIM with decorative technologies enables components with high surface finish, as well as, decorative and functional properties, among other benefits. Since the development of the technology surface improvement has been the focus of many research articles and recently, supported by the progress in machinery, technology integration has emerged as a solution. This review aims to expose the main advantages, disadvantages, and methods for surface improvement of MIM molded components. The key modifications and requirements for the tooling system as the supercritical fluid unit, the fuse, and mold modifications are discussed. The advantages of integration of these different processes with MIM technology are further described and a review of the progress so far is addressed as well as the incorporation of numerical simulation for the MIM components production. For that, technology integration of two-shot injection molding (2K Shot), In-Mold Decoration (IMD), In-Mold Labeling (IML), and In-Mold Electronics (IME), which represent the biggest integration potential with MIM are examined.
... During the cooling stage, cells can be formed in regions close to the mould walls, which decrease the thickness of the solid skin layer. Dong et al. [56] also found that the solid skin layer formation occurs at both the filling and cooling stages. However, according to these authors, the solid skin formation is mainly due to the shear flow and fountain flow during the filling phase and the cooling and polymer Silver marks are one of the two major defects of microcellular injection moulding usually shows up on the microcellular injection moulded product surface, as shown Figure 6. ...
... As for impact strength, researchers found that it could be impacted by changing both mould temperature and injection velocity [56,72]. Effectively, impact strength seems to decrease by increasing the mould temperature and injection due to the formation of a thinner solid skin layer. ...
... Effectively, impact strength seems to decrease by increasing the mould temperature and injection due to the formation of a thinner solid skin layer. However, it was observed that the melt temperature has little effects on the solid skin thickness [56]. Kastner et al. [73] investigated the biaxial bending and flexural behaviour of foamed parts after changing seven process parameters, including melt/mould temperature, degree of foaming, injection speed, delay time, gas content, and back pressure. ...
Article
Full-text available
Microcellular injection moulding (MuCell®) is a polymer processing technology that uses a supercritical fluid inert gas, CO2 or N2, to produce light-weight products. Due to environmental pressures and the requirement of light-weight parts with good mechanical properties, this technology recently gained significant attention. However, poor surface appearance and limited mechanical properties still prevent the wide applications of this technique. This paper reviews the microcellular injection moulding process, main characteristics of the process, bubble nucleation and growth, and major recent developments in the field. Strategies to improve both the surface quality and mechanical properties are discussed in detail as well as the relationships between processing parameters, morphology, and surface and mechanical properties. Modelling approaches to simulate microcellular injection moulding and the mathematical models behind Moldex 3D and Moldflow, the two most commonly used software tools by industry and academia, are reviewed, and the main limitations are highlighted. Finally, future research perspectives to further develop this technology are also discussed.
... One such challenge is silver-like swirl flow marks appearing on the part surface of MuCell. This is believed to be due to the combined effects of the partial foaming and fountain flow effects during the melt-filling process [8]. Uncontrollable and uneven foaming sizes are the other obstacle that the MuCell process encounters that further delay its usage in structural components such as automobile parts. ...
Article
Full-text available
Microcellular injection molding technology (MuCell) using supercritical fluid (SCF) as a foaming agent is one of the important green molding solutions for reducing the part weight, saving cycle time, and molding energy, and improving dimensional stability. In view of the environmental issues, the successful application of MuCell is becoming increasingly important. However, the molding process encounters difficulties including the sliver flow marks on the surface and unstable mechanical properties that are caused by the uneven foaming cell sizes within the part. In our previous studies, gas counter-pressure combined with dynamic molding temperature control was observed to be an effective and promising way of improving product quality. In this study, we extend this concept by incorporating additional parameters, such as gas pressure holding time and release time, and taking the mold cooling speed into account to form a P(pressure)-T(temperature) path in the SCF PT diagram. This study demonstrates the successful control of foaming cell size and uniformity in size distribution in microcellular injection molding of polystyrene (PS). A preliminary study in the molding of elastomer thermoplastic polyurethanes (TPU) using the P-T path also shows promising results.
... [53,54] Other researchers also recorded the average cell diameter decreasing with distance from the gate and thus an increasing CD. [9,47,51,55] Monterde, performed preliminary work with Ku-Fizz by comparing its foam microstructure to parts manufactured with MuCell. The results from Ku-Fizz evidenced CD was the highest in R1, followed by R3 and R2. ...
Article
Full-text available
The increasing demand for lightweight and economical automotive components boosts investigation of advanced materials and new lightweighting technologies. This work employs the novel microcellular injection molding technology Ku‐Fizz™. The process introduces gas with granulates at moderate low pressures into the feed zone of the injection molding machine. Ku‐Fizz is controlled by gas pressure; thus, a simple plate geometry was molded and the effect of various gas contents on the microstructure was analyzed. The material used was a chemically coupled glass fiber‐reinforced polypropylene compound. Optical microscopy was employed to measure the foam microstructure. Microcomputed tomography was used to quantify the fiber volume fraction and the orientation tensors. Results of the fully characterized microstructure showed cell density increasing and cell size decreasing with gas pressure and melt flow direction. Fiber length increased with gas content. Cell growth displaced fibers from the center of the part towards the mold surface, changing the fiber concentration and global fiber orientation.
... In this method, two or more liquid monomers or prepolymers are added to the mixing head in a certain proportion and immediately injected into the release paper or base cloth. The precise control of the production technology is also a challenge due to the special forming technology of solvent-free polyurethane synthetic leather [16,17] . another key factor. ...
... Homogeneous nucleation is a stochastic, spontaneous, additive-independent, non-pore precursor-free process of pore formation. This process is usually induced by temperature or pressure as the driving force [16,[50][51][52] . A high concentration of blowing agent is advantageous to increase the homogeneous nucleation rate, mainly because it reduces the interfacial energy [53] . ...
Article
Full-text available
Solvent-free polyurethanes are synthesized under certain conditions via a rapid reaction between liquid prepolymers. During this process the molecular weight of the polymer is rapidly increased to produce polymeric materials containing a carbamate-based structure at a very fast rate. The organic solvents are completely avoided in the solvent-free polyurethane synthesis process, thus avoiding all the problems associated with the use of organic solvents. Solvent-free polyurethane synthetic leather is extruded directly without adding solvents in the production and processing process, which has the advantages of low VOC emission and environmentally friendly. This review brings together theoretical and experimental research on the application and synthesis and preparation of solvent-free polyurethanes to generate an understanding of the theory and synthesis and preparation techniques associated with solvent-free polyurethanes. The review includes (i) the application and development direction of solvent-free polyurethane, (ii) an overview of the technology of solvent-free polyurethane synthetic leather preparation, (iii) a study of the modification and synthesis of solvent-free polyurethane prepolymers, (iv) a summary of the technology of rapid foam forming of solvent-free polyurethane and its influencing factors, (v) a review of the technology of solvent-free polyurethane synthetic leather preparation. In addition to the review, a corresponding overview of the theoretical and experimental advances in solvent-free delayed foaming technology in recent years and a summary of the technology and experience in the preparation of solvent-free polyurethanes are also presented.
... Furthermore, when injection speed is increased from 100 mm/s to 267.8 mm/s, the mean Ra decreased from 1.297 µm to 1.072 µm. This reduction in surface roughness with an increase in injection speed can be attributed to the cavity being filled earlier hence the frozen layer may have started to freeze thus mitigating the polymer/gas solution from reaching the moulding surface [43,44]. When processing with a higher melt temperature, the Ra decreased from 1.324 µm to 1.045 µm. ...
Article
Full-text available
The pursuit of polymer parts produced through foam injection moulding (FIM) that have a comparable surface roughness to conventionally processed components are of major relevance to expand the application of FIM. Within this study, 22% talc-filled copolymer polypropylene (PP) parts were produced through FIM using both a physical and chemical blowing agent. A design of experiments (DoE) was performed whereby the processing parameters of mould temperatures, injection speeds, back-pressure, melt temperature and holding time were varied to determine their effect on surface roughness, Young's modulus and tensile strength. The results showed that mechanical performance can be improved when processing with higher mould temperatures and longer holding times. Also, it was observed that when utilising chemical foaming agents (CBA) at low-pressure, surface roughness comparable to that obtained from conventionally processed components can be achieved. This research demonstrates the potential of FIM to expand to applications whereby weight saving can be achieved without introducing surface defects, which has previously been witnessed within FIM.
... Therefore, the melt must generally be subject to a temperature increase, a pressure drop or a combination of both and subsequently be able to increase its volume during foaming [127,128]. In foam injection moulding practice, usually the pressure drop in the mould cavity leads to the nucleation of foam cells [112,129]. The pressure drop induces a change of the thermodynamic equilibrium of the saturated polymer gas solution leading to a decrease of solubility of the gas within the melt [121]. ...
... At the vicinity of the injection point, the core-skin thickness is low, whereas it growths with increasing flow length. The analysis of the x-z-cross-section of an in-situ sandwich specimen illustrates the issue of flow length dependency of the foam morphology in accordance with[129]. ...
Thesis
Full-text available
Novel hybrid processes for the manufacture of continuous fibre reinforced thermoplastic (CFRTP) components have been emerging, due to increasing requirements regarding cost-efficient lightweight design especially in the automotive sector. A promising example is the in-situ CFRTP sandwich process, which combines overmoulding of thermoplastic composites with foam injection moulding. This hybrid process enables function-integrated components with high weight specific mechanical properties and complex geometry at low cycle times. However, methods for the pre�design of in-situ CFRTP sandwich components are required for the application of this process in industrial component manufacture. Therefore, several challenges must be met especially with respect to the critical aspect of interfacial bonding between CFRTP facesheets and injection moulded core as well as to the resulting weight specific mechanical behaviour depending on the material and process parameters. In this context, the present work aims to clarify the mechanisms behind the interfacial bonding development during the in-situ manufacture of CFRTP sandwich specimens. Furthermore, the relationship between process as well as material parameters and the resulting weight specific flexural behaviour of sandwich components is evaluated. This shall lay the foundation for the development of methods, which enable the mechanical modelling of in-situ CFRTP sandwich structures and thereby facilitate the pre-design of new components. For the quantitative evaluation of the interfacial bonding of in-situ CFRTP sandwich structures, suitable test methods need to be established at first. Subsequently, experimental campaigns are conducted in order to evaluate the mechanisms responsible for the development of interfacial bonding during the in-situ process. Therefore, polypropylene-based in-situ CFRTP sandwich specimens are manufactured and subsequently object of mechanical testing and analysis. After focusing on an investigation of the polymer specific bonding mechanisms, the effect of chemical and physical blowing agents on the interfacial bonding of facesheet and core is determined. In addition, the inherent lightweight design potential of in-situ CFRTP sandwich structures is evaluated, represented by the weight specific flexural rigidity. For this purpose, the foam morphology that is induced by material and process parameters as well as the corresponding weight specific flexural properties of sandwich specimens are assessed via micro computer tomography and four-point bending tests respectively. Based on these studies, model based predictive characterisations of the interfacial bonding as well as of the weight specific flexural behaviour of in-situ CFRTP sandwich structures are developed and evaluated using experimental data. In order to demonstrate the applicability of the developed models in the pre-design of in-situ sandwich components, they are used for the substitution of a steel reference component. This shall further highlight the promising potential regarding cost-efficient lightweight design of in-situ CFRTP sandwich structures.