1. Introduction
Due to a wide range of beneficial properties, synthetic polymers generally derived from fossil fuels are in widespread use, as over 390 million metric tons of plastic are produced globally [
1]. One property, which has turned out to be something of a curse, is that most plastics have great durability and are resistant to degradation, enabling them to persist as environmental pollutants for hundreds of years [
2]. When not properly disposed, plastics can cause environmental pollution [
3], harming wildlife and ecosystems, [
4] as well as humans [
5,
6]. Therefore, it is important to manage the waste plastic and recycle it to minimize the harm caused by wasted plastic to benefit both the environment and humanity [
7]. Unfortunately, only 9% of plastic has been recycled [
8]. Of the rest, half is landfilled, 22% is mismanaged, and 19% is burned or incinerated [
8]. Of the unrecycled plastics, thermoplastics present a substantial opportunity to profitably utilize available materials, reduce pollution, and redirect waste from landfills. A new approach to developing a circular economy for plastics is being developed in the additive manufacturing industry (AM). It has been shown to be profitable [
9,
10] using the process of distributed recycling for additive manufacturing (DRAM) [
11,
12]. In this model, prosumers (a portmanteau of producing consumers) have a direct economic benefit by offsetting purchase of plastic products by recycling their waste into custom open-source products [
10]. This model is in contrast to traditional centralized recycling models for plastic, which provide no incentive to consumers because of the low value of low density of collecting and transporting post-consumer plastic waste [
12]. DRAM plastic converted to AM feedstock will increase in value between 4x and 20x as the value of bulk commercial plastic pellets (
$1-5/kg) or commercial filament (~
$20/kg). With DRAM, greenhouse gas (GHG) emissions from the embodied energy of transportation are minimized for AM materials [
13,
14]. This result is possible in the most extreme case of consumers manufacturing their own products from their own waste in their own homes [
15,
16]. Further reductions in GHG emissions are possible when DRAM uses renewable energy like solar photovoltaic technology [
17,
18]. Community-level DRAM using a recycling network is also feasible [
19,
20] and still more efficient than centralized recycling [
21]. Overall, DRAM models challenge global value chains already under assault with distributed manufacturing [
22].
In order to facilitate DRAM, open source (OS) waste plastic extruders called recyclebots [
23,
24] have been developed to provide filament feedstock for Fused Filament Fabrication (FFF) processes. Recycled waste plastic filaments can be used in any low-cost self-replicating rapid prototype (RepRap)-class [
25,
26,
27] 3D printer. A wide range of recycled plastic has already been shown to be DRAM compatible:
polylactic acid (PLA) [
28,
29,
30],
acrylonitrile butadiene styrene (ABS) [
10,
31],
high-density polyethylene (HDPE) [
23,
32,
33],
poly(ethylene terephthalate) (PET) [
34,
35],
linear low-density polyethylene (LLDPE) and low-density polyethylene (LDPE) [
36,
37],
polypropylene (PP) and polystyrene (PS) [
33],
carbon-reinforced plastic composites [
39],
waste wood fiber reinforced plastics [
35,
40]
fiber-filled composites [
41,
42].
Furthermore, the filament-making step can be avoided by 3D printing directly from shredded waste in Fused Particle Fabrication (FPF) / Fused Granular Fabrication (FGF) systems [
43,
44]. Using direct screw-assisted extruders, either single- or twin-screw systems, further expands the range of available DRAM materials [
1,
45], including polymer blends and multi-material recycling thermoplastics [
46,
47], multiple-recycled flake feedstocks [
43,
48], and bio-based thermoplastics or composites [
49,
50,
51]. Moreover, it improves the economics of DRAM [
47,
51,
52], reducing the cost of producing the material and environmental pollution [
54].
There are, however, challenges remaining in DRAM, especially focusing on the materials qualification step. For example, different types of polymers require distinct recycling processes, making proper sorting essential [
55]. Impurities, contaminants, and the complexities of recycling multi-polymer waste streams pose significant challenges due to incompatibility issues. These impurities affect overall processability, such as flowability and printability, and diminish technical properties, e.g., mechanical and rheological properties. At the same time, incompatibilities increase material heterogeneity, making it difficult to accurately predict changes in properties. For unknown plastics of different types, rapid characterization methods can help to identify the potential processability of the material to be used in DRAM, reducing the impacts and scraps generated in the initial tuning of the 3D printing setup. One proposed method is the melt flow index (MFI) measurement, which is a good reference for the melt flow behavior of a thermoplastic material, hence its flowability during the 3D printing process [
56,
57]. MFI, or melt flow rate (MFR), measures the ability of the molten polymer mass to flow through an orifice or die below a heated barrel under a given loading pressure and temperature for a given amount of time [
58], usually measured in g/10min. MFI is a proxy index feature related to the material’s molecular weight [
59], which means it can provide information about the material’s viscosity and flowability, allowing a better understanding of its potential behavior in the 3D printer [
55]. It should be noted that MFI is measured at a low shear rate compared to the real stress during 3D printing. In general, the higher is the MFI, the lower are the viscosity and molecular weight of the tested material, increasing the flow per unit time. This value can be used to determine other properties, e.g., melt volume rate (MVR) and intrinsic viscosity, giving further insight into the rheological behavior of the material [
60]. MFI also helps set an initial melt temperature without the need for more complex characterization methods, such as differential scanning calorimetry (DSC). Although other thermal properties also affect printability in FFF/FGF, e.g., crystallinity index [
61], the immediacy of MFI measurements and the availability of standardized methods make it an accessible and reliable way to assess the printability of thermoplastics [
62]. For DRAM operationalized at the community scale, MFI represents a potential means to quickly screen potential AM feedstock materials [
56,
63], as the material characteristics could be changed after one or multiple recycling processes due to thermomechanical degradation of thermoplastics during the recycling and extrusion steps [
43,
64]. For example, the MFI of ABS will increase after recycling due to degradation, leading to a decrease in its viscosity [
65], and hence, its flowability increases. Thus, new 3D printing temperatures or speeds may be applied. In addition, MFI is not only used to assess the behavior of pure thermoplastic materials; it also provides a quick evaluation of the flowability and printability of materials that contain additives, such as compatibilizers [
66], chain extenders [
67,
68], fillers [
69], and bio-sourced components [
70,
71], further expanding its use.
To rapidly assess the printability of recycled materials, MFI presents a viable and rapid alternative to complex and longer rheological measurements [
72,
73]. Unfortunately, proprietary MFI systems are still expensive, ~CAD
$4,700 from Amazon [
74] and ~CAD
$2,000 from AliExpress [
75]. This fact limits accessibility to resource-constrained settings for which DRAM is perhaps the most promising because prosumers could trade their labor for high-value products for themselves or to sell. Furthermore, exploiting rapid characterization tools for DRAM could improve the overall quality of the 3D printed products produced by the prosumers, hence increasing the adoption of this technology and its reliability for product applications, e.g., reducing failures and material scraps from parameter tuning.
To address this issue, this article introduces a low-cost open-source Melt Flow Index er. First, the basic functioning of an MFI is outlined. The operation and design of each of the major subassemblies of the OS MFI device are then detailed. The complete bill of materials (BOM) and assembly instructions are provided in
Appendix A and
Appendix B. Next, the OS MFI device is validated against a gold-standard commercial MFI and then used for the MFI assessment of some common thermoplastics, including waste plastics for DRAM: virgin PLA pellets, shredded recycled poly(ethylene) terephthalate glycol (PETG) flakes, and recycled HDPE/ PET flake blends. The results are compared and discussed in the context of DRAM.
2. Materials and Methods
An MFI device is a measuring tool, which can measure the MFR of a thermal-sensitive polymer material. An MFI device normally comprises load weights, a piston, a heated barrel with a die, a cutter system, and a scale. Usually, the procedure of measuring MFR acts by these steps: first, heat up the barrel to the desired temperature; second, add the polymer sample into the heated barrel and wait for a certain time until the sample melts, i.e., preheat time; third, put the weight on the top of the piston then after a certain period of time, measure the mass of the extrudate forced to pass through the die. Before and after the tests, the barrel and die should be cleaned to ensure no contamination and repeatability of the tests, which usually follow ASTM or ISO standards to define timings, temperatures, weight, and dimensions of the main MFI components [
60]. Among the common commercialized MFI systems, some of them are cumbersome to operate and are not automated. For example, the MFI products from MRCLAB need operators to put the weight on the top of the instrument and count down the time [
76]. Normally the operator needs to collect the samples and weigh them afterward, such as for many melt flow indexers on AliExpress [
75]. To address this issue, the open-source MFI designed in this article was developed to be mostly automated. In the proposed design, the OS MFI can apply loads automatically via the DC motor, cut the extruded material, and weigh it automatically.
To fulfill the functionality of the MFI, the system here described relies on mechanics, electronics, and free and OS software, all of which are available on the Open Source Framework [
77]. The BOM for the make, mechanical, and electronical parts are included in
Appendix A. The mechanical components are composed of aluminum extrusion profiles, 3D printed parts, and fasteners. The overall structure is a vertical frame that holds a cylinder, which works as the heated barrel to melt the sample materials. In the electronic part, the instrument is controlled by a Teensy 4.0 board [
78], and temperature control, motor, and digital scale systems are integrated into one control system. The whole process will be controlled by the code upload to the teensy board to make it easy to operate and automatic. The cutter on the MFI device can cut the extrusions at set intervals to automatize the extrudate collection from the die, and the digital scale can weigh them and record data. Finally, the device designs are meant to be open source, hence digitally replicable and low cost. All the buy components used for the hardware design are readily available on the market. Custom parts are designed to be quickly produced with low-cost desktop-size FFF 3D printers and commercial filament feedstock, i.e., PETG and polycarbonate (PC). The structure of the frame is designed to optimize material usage, hence, to be produced with less material and require a limited amount of buy components. For this reason, far less machining is needed than conventional MFI devices, further reducing costs.
2.1. Mechanical System
The framework consists of two 20x20 mm aluminum profiles, 75 mm and 30 mm long, respectively, and some 3D printed parts. This framework connects the different subassemblies together and keeps the whole structure steady. Compared to commercial MFI products, this design uses a stepper motor as the weight on the top of the piston. With the linear rail, the shaft of the motor can move up and down on the same track, which helps decrease the vibration on the motor rod. The piston is made of a piston head and a piston rod, and the piston head has a multi-layered structure, which consists of two nuts, one O-ring, and one washer. The O-ring keeps the piston head from leaking. The piston rod is a threaded steel rod, it allows the piston head to screw on it. There is a button shape load cell between the motor shaft and piston rod, which can measure the pressure so that there is a feedback loop for the motor to keep the same pressure. The barrel for heating up samples is a 304 stainless steel pipe, which can be found easily on the market. A copper cap with a hole is then added to the barrel to act as the die. A PC insulation housing with heat insulation cotton material covers the whole heated barrel to ensure heat stability. Below it, there is a servo motor equipped with a blade that acts as the cutter for the material samples to be weighted. The overall design of the mechanical system of the MFI device is shown in
Figure 1, and the BOM is visible in
Appendix A.
2.2. Electronics
To control the system, there is a Teensy 4.0 board that acts as the control board. The control system, as shown in
Figure 2, can be divided into two main parts, which are the heating system and the motor force control system. As mentioned above, there is a feedback loop for the motor. When the force does not reach the desired value, the current of the motor will increase so that the torque output of the motor will increase. PID control is applied to the heating control system. All the terms in the PID control system need to be adjusted according to different situations. For example, if the overshot is too high, then it can be improved by reducing the portion term. This system itself runs automatically, but all the input parameters like time, temperature and pressure need to be input manually in the code or firmware. There are two modes in the code, which are auto mode and manual mode. Manual mode is meant for adjusting the position of the piston head, and cleaning procedure after measuring process.
2.3. Testing and Validation
2.3.1. Calibration Process
Before testing or validation, the tester needs to be calibrated to ensure precise testing results. There are three subsystems that need to be calibrated: 1) the force control system, 2) the temperature control system, and 3) the cutter system.
In the force control system, the load cell between the motor rod and the piston needs calibration. It can be calibrated by using a known weight, and a calibration factor can be obtained after this process. The detailed operation instructions are included in the calibration code in OSF [
77]. To perform the calibration correctly, a 3D printed calibration part should be applied (
Figure 3 and
Appendix A, part 19). The calibration factor may change after installation and needs to be checked before testing.
For the temperature control system, the two heating elements of the OS MFI system need to be calibrated to ensure the temperature is the same in the heated barrel and the cap. It can be done by using another temperature sensor as a reference, for example, an additional thermocouple previously calibrated. The temperature is stable in the heated barrel of the OS MFI system, but there is about a 5-degree gap between the inside and outside of the cap, requiring an adjustment of the temperature setpoint on the cap. This fact may be due to different heat loss rates of the parts or insulation issues on the cap, making calibration important to reach stable and precise temperature values.
The movement of the cutter system can be adjusted in the code in terms of cutting time interval or moving range of the tool. As the position of the blade may affect the cutter performance, it needs to be adjusted before the testing process manually. For instance, it can be adjusted by moving the cutter-fix part until touching the bottom of the cap with the blade.
2.3.2. Validation Process
The operational instructions of the OS MFI device are detailed in
Appendix B. To validate the use of the OS MFI, a series of experiments was designed to compare the measurement results of the OS MFI system with a commercial product available on the market. Compared to the commercial versions, the design of the proposed OS MFI device has some differences, e.g., the diameter and length of the heated barrel, from the specifications in the standardization documents, such as ISO-1133 [
80] and ASTM D1238 [
81].
The design of experiments follows the principles of a controlled variable experiment. Except for the difference in testing systems, all other experimental conditions, such as the testing parameters and the materials, are kept consistent. To compare the developed MFI with its commercial counterpart, an Instron CEAST MF20 machine (Instron, Norwood, MA, US), located at the LRGP laboratory in Nancy, France, was utilized following the ASTM D1238 [
81] standard.
Materials were obtained from various sources, including virgin pellets, recycled plastic waste, blend combinations with compatibilizers, and shredded 3D printing waste from the laboratory. They were dried at 60 °C for two days before the test. Virgin PLA pellets were supplied by NatureWorks (Savage, MN, USA) with a specific gravity of 1.24 g/cc. Recycled HDPE/PET flake blends were obtained from water bottles coming from the French brand Cristaline and processed at the ERPI laboratory in Nancy, France. This material comprised 10 wt% HDPE (cap) and 90 wt% PET (body), hereinafter called rPET90/rHDPE10. The same recycled material was tested with an addition of 10 wt% styrene-ethylene/butylene-styrene block copolymer (SEBS) G-1652 containing approximately 30 wt% polystyrene units (rPET90/rHDPE10/10SEBS), kindly donated by Kraton Polymers (Almere, Netherlands). Additionally, recycled PETG from shredded 3D printing waste at the FAST laboratory was tested. The shredded waste parts were originally fabricated using virgin PETG filaments provided by Polymaker (Shanghai, China).
To ensure the reliability and repeatability of the process, the analysis was performed on three samples of approximately 5 g for the commercial and 10 g for the developed OS MFI. The materials were tested at temperatures of 190 °C for virgin PLA, 220°C, 230 °C, 240°C for recycled PETG, and 255 °C for rPET90/rHDPE10 and rPET90/rHDPE10/10SEBS, using a 2.16 kg weight. The measurement procedure can be found in
Appendix B.
3. Results
Table 1 presents the results obtained from virgin PLA, rPET90/rHDPE10, rPET90/rHDPE10/10SEBS, and recycled PETG using both commercial and OS machines. The results were then compared with the data sheets of the virgin materials for PLA and PETG filament, as well as values from the literature on 3D printed PLA [
39,
56,
82,
83], PETG [
84,
85,
86], HDPE and PET [
70,
87]. It can be observed that the MFI of PLA assessed with the commercial device corresponds to 6 g/10min and a relative standard deviation of ~13%, demonstrating both the precision and accuracy of the commercial machine. In contrast, the OS machine exhibited a 15% value decrease compared to the commercial machine despite a better relative standard deviation, i.e., ~5% when the preheating time is 10 minutes, and a comparable value with ~19% standard deviation when the preheating time is 13.5 minutes. The results are comparable with the state-of-the-art, which shows significant variations in the MFI values, also influenced by the different feedstock batch and grade, i.e., molecular weight and additives of the specific formulation. For instance, Wang et al. obtained MFI of ~4.3 and ~11.1 g/10min at 190 °C and 210 °C [
56], whereas Nasir et al. reached ~11 g/10min at 190°C [
83]. Tian et al. reported values of ~2 g/10min at 180 °C, which significantly increased at 240 °C [
39]. In general, MFI values of 3D printed PLA range between 6 and 10 g/10min [
82], confirming the reliability of the results obtained from the commercial and OS MFI devices.
Regarding PETG, the filament datasheet indicated MFI values of 3.9 g/10min and 10.8 g/10min at 220 and 240 °C, respectively. The value obtained with the commercial machine is 9 g/10min at 230 °C with a relative standard deviation of ~6%. This MFI value is within the range of the commercial virgin filament [
88], suggesting that the 3D printing and shredding processes do not significantly impact material degradation. Similarly, the MFI obtained with the OS machine fell between the two values from the datasheet, showing a decrease of ~23% compared to the commercial machine. As for PLA tests with the OS MFI, the values are in line with the state-of-the-art, where results of ~10.5 g/10min have been reported at 240 °C [
84]. To ensure comparability with the datasheet, the tests were also conducted at 240°C. The MFI recorded from the commercial machine was 14.3 g/10 min, while similar values were found for the OS MFI, with a value of 13.6 g/10 min. This slight increase in MFI may be attributed to minor degradation of the material during the process. The test conducted at 220°C yielded values of 6.5 g/10 min and 4.2 g/10 min for the commercial and OS MFI, respectively, with this decrease possibly attributed to inherent variability in the testing process; significant variability in the results was also reported for PETG. For example, Vijayasankar et al. reported an MFI of ~20 g/10 min at the same temperature [
85]. Kotomin et al. compared the MFI values of PETG from different temperatures, obtaining ~15 g/10min at 240°C and more than 30 g/10min at 250 °C [
86]. For this reason, the values from the measurements with the commercial and OS devices can be considered reliable, confirming the validity of the OS machine.
The HDPE/PET blends derived from the plastic bottle waste stream showed MFI values of 34.5 g/10min without compatibilizer (rPET90/rHDPE10) and 31.1 g/10min with compatibilizer (rPET90/rHDPE10/10SEBS) when tested with the commercial device. Compared with the OS device, it can be observed that MFI is ~15% higher and ~34% lower with compatibilizer and without compatibilizer, respectively. Considering the lack of direct comparison from the state-of-the-art, some considerations can be made by checking the MFI values reported for HDPE and PET. Previous works obtained MFI values ranging between 3.5 and 40g/10min for PET, showing a significant variability given by the pre-heating conditions [
87,
89,
90]. HDPE MFI values from the literature also exhibit the same trend [
59]. Nevertheless, the results from the commercial and OS MFI devices are comparable, indicating the reliability of the OS machine in testing novel material compositions and plastic blends.
When dealing with data from the OS MFI device, only the last ten sets of data are accepted. According to
Figure 4, there is a clear increasing trend of extrusion weight through time for PLA, and all the tested materials show a similar trend when using the OS MFI device. However, the results for commercial equipment do not show this trend. One factor that can cause this phenomenon is the difference between the real temperature inside the die and the nominal one at the beginning of measurement. It may be due to insufficient insulation on the bottom of the cap, which can cause heat loss and less thermal control. The difference in materials between the cap and the heated barrel can also lead to differences in heat transfer, requiring a calibration step of the temperature control system (
Section 2.3.1). A preload process may be needed for a more precise result. For example, the first few samples flowing from the die can be discarded as part of the preload process, and the number should be determined through preliminary tests with specific materials. Due to a higher sample mess used in the OS MFI, the whole testing process may take a longer time, which can increase material degradation and affect the results.
Multiple experiments were done to verify this phenomenon through OS MFI, as shown in
Figure 5. Accordingly, the material is fully heated in ~8 minutes. The results show a clear linear increasing trend with the increase in pre-heating time. Therefore, it is important to keep a constant sample weight throughout the tests. Moreover, according to the standard file ISO 1133, material in flake or powder shapes should undergo a preprocess, i.e., a pressing process with a vacuum pressing tool to evacuate air in samples. This step will reduce the degradation of material caused by oxygen. This fact also explains the severe degradation shown by the rPET90/rHDPE10 measurements.
Overall, as shown in
Figure 6, both systems showed similar measurement precision and were capable of stable operation within a standard deviation of ~5-20%. Although calibration is required, the results indicate that the OS MFI system can measure the MFI of different materials with precision comparable to commercial MFI devices. The data obtained from the OS MFI system can be useful to observe and make relative comparisons of different melt materials or temperatures, outlining the overall behaviors of each processed feedstock. Additionally, the study demonstrated the use of the OS MFI with different thermoplastic materials, either virgin or recycled. Compared to the PLA test data, there is a larger difference between the weight of extrudates made of PETG and HDPE/PET blends. This phenomenon could be due to the substantial differences in shape and size of the shredded PETG and HDPE/PET blends, e.g., different granulometries and dimensional ratios between pellets and shredded flakes, leading to the formation of voids during extrusion, thereby affecting the measurement results and increasing their variability [
80,
92].
4. Discussion
At the community scale, developing a distributed recycling process required the whole value chain to be adequate, from waste-to-product. In that sense, qualifying the plastic waste stock in a quick and efficient manner represents a challenge for the implementation of this process in a particular territory. The melt flow index MFI measurement represents a potential means to resolve this issue.
The OS MFI device developed in this research offers an accessible and low-cost way to rapidly assess the flowability and printability of recycled thermoplastic materials and blends. To validate the accuracy of the OS machine, a comparison was conducted with a commercial MFI device and the state-of-the-art. The results show differences with both the OS MFI system and commercial device compared to the datasheet and the literature. The measurement of the MFI can be significantly affected by the feedstock grade, e.g., molecular weight and specific additives, but also by different parameters such as temperature, load weight, the diameter of the die, the diameter of the barrel, and their cleanness [
50,
63], as well as the heat transfer conditions in the whole device itself. For instance, increasing the testing temperature of 10 °C can lead to a two- or three-fold increase in the MFI values, such as for PETG feedstock [
86]. Moreover, as shown in the results part (
Section 3), the pre-heating conditions can also significantly modify the results, e.g., with differences of one order of magnitude [
87]. Despite equal temperatures and load weights, the diameters of the barrel and die might impact the measurements, as well as the properties of the materials used for these components, e.g., different heat capacities and specific heats [
56]. Changes in these factors reasonably explain the differences in the test results between OS and commercial MFI devices. Likewise, inconsistencies can be found regarding the MFI test results in the literature, even for similar materials used from variability in material grade. For instance, Singh et al. reported an increase in the MFI of recycled ABS [
55], whereas other works demonstrated a decrease in the MFI of the same material [
72,
73]. Again, these contradictory results highlight the variability in MFI values, which may be influenced by differences in experimental conditions, material processing, measurement techniques, or the measuring equipment used in these studies, as well as different feedstock grades and tested batches. Furthermore, according to Rides et al., MFI measurement has larger differences between different laboratories [
64], confirming the variability in the equipment conditions, environment, e.g., room humidity, and setup, especially for polar and relatively polar materials.
Providing the whole code for the OS MFI could help overcome this challenge, ensuring that any research lab, community makerspace, or other DRAM facility could use nearly identical systems. Compared to standard commercial MFI devices, the OS MFI developed in this study utilizes a DC motor to apply the load weight, which can impact the measurements, as load weight is a critical parameter. From a user perspective, this feature can simplify the operation and enhance the safety of the measurement process, making it more accessible and repeatable in DRAM contexts. It is important to highlight that MFI is a valuable tool for the rapid assessment of the flowability and potential printability of materials. For more detailed and scientifically rigorous results, however, comprehensive rheological analysis using rheometers should be conducted even when using commercial MFI devices. These tests can help better understand the behavior of the molten material under high shearing, such as in 3D printer extruders. Furthermore, MFI can not only be used in DRAM contexts or recycling activities but also in laboratory environments [
94]. This choice can help make research more affordable and reliable because this characterization can support the fine-tuning of 3D printing parameters with novel material formulations, helping to ensure extrudate consistency and, hence, improving the technical properties of the final parts, e.g., achieving better mechanical properties by reducing voids and defects from extrusion inconsistencies.
There are limitations of the OS MFI device that need future work. Currently, cleaning procedures are labor intensive. The cap needs to be disassembled to clean it from the inside, requiring the disconnection of the band heater and thermocouple. Creating or identifying specialized cleaning tools to simplify the cleaning process could reduce the difficulty of cleaning. Furthermore, the temperature control system could be improved in accuracy as it currently shows variations of ~2 °C. Although there are two heating systems, the nichrome wire, and the band heater, temperature difference still exists in the MFI device, leading to different MFI values according to the specific pre-heating times (
Figure 5). For example, the temperature in the die on the cap could be lower than other parts, e.g., 170 °C instead of 190 °C, affecting its accuracy. Future experiments could also consider the thread of the cap. Due to the threaded fit of the cap and the pipe (National Pipe Taper, NPT), the cap cannot thread all the way up. This constraint leaves a part of the thread exposed, and it can affect the shear force when extruding, potentially influencing the beginning of the measurements. This thread type, however, helps prevent leakage, increasing accuracy and limiting the shear force effect.
To have better accuracy, some improvements can also be made to the device. According to the previous test at 190°C, the position of the band heater significantly modifies the actual temperature in the die. If the position of the band heater is up, roughly where the bottom of the cap can be exposed, the temperature in the die will be 170 °C, while if the position of the band heater is down, roughly where the cap can be completely covered, the temperature will be 182 °C. This test shows that the relative position of the band heater and cap affects the temperature inside the die, showing a significant improvement after fixing the position of the band heater and the cap. These results indicate that the stability of the temperature is a key factor in getting a more accurate MFI measurement. Hence, further accuracy improvements might be made by reinforcing the insulation layer and having a more advanced temperature control system, including improved insulation, temperature sensors, or advanced temperature control algorithms. The accuracy of the digital scale and its interaction with the cutter system can also impact results. In the current OS MFI device, the weight is unevenly distributed on the scale plate, leading to potential measurement errors. Improvements in scale and cutter design can, therefore, increase accuracy. A better motor control system can also be considered in future versions of the OS MFI device. Current motor control systems are generally accurate and can introduce some errors in the pressure. Therefore, using more advanced motor control algorithms [
95] can make the pressure more accurate, making the results more accurate as well. Finally, future work could include a Graphical User Interface (GUI) to make the system easier to operate and guide data interpretation and analysis, especially for non-expert users or DRAM contexts.
5. Conclusions
To address the current issues with MFI systems, a low-cost OS MFI device was developed. MFI Measurements of virgin PLA pellets, recycled PETG flakes, and HDPE/PET blends were carried out using the developed device, showing good measurement precision with a ~5-20% standard deviation. Compared to its commercial counterpart, it has a ~5-23% decrease in PLA and PETG measurements, which shows a similar trend. The OS MFI can be a valuable characterization tool for easily sorting different material feedstocks, determining their suitability for FFF/FGF 3D printing, and identifying the optimal 3D printing temperature. This study demonstrated the development and use of an OS MFI with performance comparable to its commercial counterparts. The validation test reported similar MFI values for both the commercial and OS MFI devices when using common 3D printing feedstock, i.e., virgin PLA and recycled PETG, and new polymer blend formulation from plastic waste, such as HDPE/PET blends. Some challenges remain, however, particularly in achieving consistent temperature along the heated barrel and die. Therefore, future machine versions should improve the temperature control system and connection between the cap (die) and heated barrel, optimizing the heat transfer in the whole equipment, e.g., improving insulation or changing part of the buy components selected for the current version. To enhance user-friendliness, future work can develop a graphical user interface, guided testing and analysis procedures, and accessible tutorials that enable the adjustment of test parameters, such as pre-heating, weight load speed, or automated cutting timings.
The MFI devices in the market are currently expensive. An OS MFI device can make the recycling process easier and more efficient, becoming a valuable option in different contexts, such as DRAM and laboratory environments. A more affordable and accessible version of MFI devices can help enable DRAM to become more widespread and trustable in terms of material manufacturing processing.
Author Contributions
Conceptualization, H.B. and J.M.P.; methodology, D.L., A.B., C.S.G.; software, D.L.; validation, D.L., A.B., C.S.G., A.R.; formal analysis, D.L., A.B., C.S.G., A.R., H.B, C.N., F.A.C.S. and J.M.P.; investigation, D.L., A.B., C.S.G., A.R.; resources, H.B, C.N., F.A.C.S. and J.M.P.; data curation, D.L.; writing—original draft preparation, D.L., A.B., C.S.G., A.R., and J.M.P. ; writing—review and editing, D.L., A.B., C.S.G., A.R., H.B, C.N., F.A.C.S. and J.M.P.; visualization, D.L. and A.R.; supervision, H.B, C.N., F.A.C.S. and J.M.P.; project administration, J.M.P.; funding acquisition, H.B, C.N., F.A.C.S. and J.M.P. All authors have read and agreed to the published version of the manuscript.