Open Access
Review
Issue
Manufacturing Rev.
Volume 8, 2021
Article Number 14
Number of page(s) 17
DOI https://doi.org/10.1051/mfreview/2021012
Published online 29 April 2021

© F.M. Mwania et al., Published by EDP Sciences 2021

Licence Creative CommonsThis is an Open Access article distributed under the terms of the Creative Commons Attribution License (https://creativecommons.org/licenses/by/4.0), which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

1 Introduction

According to ASTM standard (ASTM F2792-12a), additive manufacturing (AM) is described as a set of technologies that are utilized to generate 3D parts from computer data, usually by adding layer upon layer of material, as opposed to the subtractive methods that involve removal of material during the fabrication process [1]. The technology is one of the major components of the 4th industrial revolution [2]. As a result, significant research has been channeled towards various AM technologies. Polymer laser sintering is a subset of additive manufacturing technologies. The PLS process involves the consolidation of material powder with the use of laser energy [1]. This AM technique is one of the most promising technologies for processing polymers because of its capability to print components with excellent surface finish, good mechanical properties, high durability and high dimensional accuracy. Moreover, the process does not require support structures as the powder provides this, which eliminates the need for post-processing upon removal of the printed part [3]. Uptake of the method is, however, obstructed by a limited variety of applicable polymers. The dearth of a wide array of PLS polymeric materials is attributed to the stringent processing conditions as well as material-property requirements of the process [1]. The processing conditions of PLS include optimum process-chamber temperature, suitable extraction-chamber temperature, appropriate scanning speed and laser power [4]. Moreover, polymers for the PLS process should have acceptable intrinsic and extrinsic properties [1]. Intrinsic characteristics include thermal, rheological and optical properties, whereas the extrinsic attributes encompass particle size, particle morphology and powder density [1]. These conditions and requirements have contributed to the limited palette of polymeric materials available for the PLS process. Of the PLS polymeric materials available, 90–95% are either polyamide 12 (PA 12), polyamide 11 (PA-11), or their blends [5]. The balance are polymers such as polypropylene (PP), polyether ether ketone (PEEK), polyethylene (PE), thermoplastic elastomers (TPE), and polyurethanes (PU), as represented in Figure 1 [1]. Therefore, there is a need for more research to be carried out to broaden the choice of polymeric materials for PLS.

In the recent past, considerable research efforts have been channelled towards the development of new powdered polymers with the aim of broadening the spectrum of PLS polymeric materials [5]. It is essential to characterize newly developed polymeric materials before processing them to determine their suitability which raises the need for well-established techniques for the characterization of powder. There is also a need to recycle the unsintered polymer powder because in PLS processing only about 5–20% of the supplied powder is utilized [6,7]. The remaining powder acts as the supporting structure for the printed components and general filling of the build platform. Furthermore, due to the limited choice of PLS polymers, the cost of the available polymeric materials is very high, thus further broaching the need to recycle the unused powder [8]. According to Mägi et al. [7], the cost of PA 12 is about $150 per kilogram, while the cost of an equivalent polyamide feedstock for injection molding is about $3 per kilogram. Therefore, it is critical to recycle the unused powder to reduce production costs.

The PLS technique results in the degradation of polymers due to exposure to high temperatures for extended periods of time [7,9]. It is imperative to investigate the degree of degradation of polymeric powder after each processing cycle to determine its viability for re-use. Powder characterization is required to ensure the building of products with known and repeatable properties [9] and it is important to have knowledge of the various methods of characterizing polymeric powders that are used in PLS. Some of these methods include differential scanning calorimetry (DSC), thermogravimetric analysis (TGA), laser diffraction analysis, gas pycnometry, scanning electron microscopy (SEM), and melt flow index (MFI) testing [5,10]. This paper presents a review of commonly used techniques for the characterization of polymeric powders that are used in the PLS.

thumbnail Fig. 1

Percentage distribution of polymers applicable to the PLS process [1].

2 Overview of the PLS process for polymers

Polymer laser sintering is one of the common types of AM technologies. This technology was invented by Carl Deckard and Joseph Beaman at the University of Texas, Austin [11]. The technology was commercialized by the DTM Corporation and EOS GmbH Electro Optical Systems in 1992 [11]. It involves the use of a laser beam to fuse powder particles together. The technique is applicable to a wide variety of materials ranging from metals, composites and ceramics to polymers [11]. Therefore, PLS is a widely applied AM technique.

The PLS technology is a matured prototyping as well as a manufacturing technique. A typical PLS machine is shown in Figure 2. Laser sintering of polymers comprises three steps, that is pre-heating, building, and cooling phases [3]. The pre-heating phases involve warming of the machine and polymeric powder (in the build chamber, as shown in Fig. 2) to temperatures just below the melting point of the material using a set of heaters placed around the build chamber. The building phase involves heating the polymeric powder using a laser beam to melt and fuse the particles following the geometry of a part to be printed. After each scanning cycle, the building platform is lowered by one-layer thickness and the process is repeated until the entire component is printed. The building phase is carried out at a constant temperature which is achieved by the set of heaters mentioned above. The third stage involves cooling and solidification of the printed components, the temperature of which is controlled through the use of another set of heaters placed along the sides of the extraction chamber, as shown in Figure 2. This is done by gradual cooling to prevent warping of the built parts. Nitrogen gas is also pumped into the built chamber during the three processes to reduce the degradation of the material as well as to minimize oxidation [12]. Laser sintering of polymers is a high-temperature process, the heating profile of which is summarized in Figure 3.

In Figure 3, the symbol Ts is the starting temperature, TB the building temperature, TE the extraction temperature, and tBC the combined building and cooling time. The combined building and cooling times are subject to the distribution, volume, and height of the parts being printed [3]. The curves in Figure 3 show that polymers are subjected to high temperatures during the entire PLS process. This exposure alters the properties of the polymers which influence the recyclability of the unsintered powder [13]. In addition, degraded powder compromises the quality and mechanical integrity of the printed parts [14,15]; hence, the need to characterize the used powder before re-using it to determine the degree of degradation.

thumbnail Fig. 2

A schematic representation of an PLS machine (EOSINT P380 Machine).

thumbnail Fig. 3

The heating profile of polymeric material during PLS [3].

3 Properties of suitable polymers powders for use in PLS

Polymers applicable to the PLS process should possess suitable intrinsic and extrinsic properties [5,14]. Extrinsic properties describe the physical characteristics of the polymers including powder density, particle size distribution and morphology. The intrinsic properties of the polymers consist of thermal, rheological and optical properties [16]. The thermal behaviour of polymeric powders includes melting point, sintering window, and temperature degradation point [13,14]. The rheological properties include the viscosity and surface tension of the material [13,14]. The optical characteristic determines the absorbing behaviour of laser energy [13,14]. The techniques for characterization of powder are based on the abovementioned intrinsic and extrinsic properties.

3.1 Particle size distribution and morphology

Particle size distribution and morphology need to be optimized for PLS powders. Suitable PLS polymeric powder particles should be near-spherical in shape to encourage as near free-flowing characteristics of the powders as possible [17]. Moreover, appropriate PLS polymer powders should have a powder distribution of between 20 and 80 μm [17,18]. Extremely small particles induce stickiness which reduces flowability [17]. Flowability of the powder determines uniform spreading of powder on the building bed. It is also crucial in PLS because it determines how layers are deposited across the build chamber. The layers should be uniform to ensure homogenous properties of the printed parts [19]. Lack of homogenous layers promote porous and weak components [20]. This may furthermore lead to distortion of the parts during laser sintering with the result that the recoater may catch on the parts and dislodge them from the powder bed. On the other hand, extremely large particles affect the spreading of the powder using a roller or blade. Large particles also discourage fusion which introduces porosity and in turn reduces the mechanical integrity of printed parts [21].

3.2 Thermal properties

Appropriate thermal properties are essential for the successful processing of semi-crystalline polymers using PLS. Polymers should have a high-temperature degradation point because PLS occurs under high temperatures [13]. The processing temperatures should be maintained between the melting point and the crystallization point of polymeric materials to prevent uneven solidification of the printed parts which might affect the geometrical accuracy as well as the surface finish of the manufactured components [8,13]. The difference between the melting point and the crystallization point of a polymeric material is referred to as the sintering window [8,13]. Suitable polymers are characterized by a wide and sufficient sintering window which prevents crystallization of the polymers during processing [8,13]. Rapid crystallization of the printed components is a major hurdle in PLS because it encourages curling, which in turn affects the surface finish and dimensional accuracy of the produced parts [17]. Furthermore, suitable polymers should have a narrow melting point range to prevent the use of high laser energy when fusing the powder particles [8]. High laser energy leads to greater degradation of the powder supporting the components being printed which hampers the recyclability of the material [13]. Therefore, thermal properties do significantly determine acceptable polymers for the PLS process.

3.3 Rheological properties

Viscosity and surface tension also determine the applicability of polymers in the PLS process. A suitable polymeric material should have low viscosity and low surface tension to ensure adequate coalescence of the powder particles [17,22,23]. Unlike injection molding, PLS does not provide additional compacting; therefore, it is important that the material has low melt viscosity with zero shear stress [17]. Low surface tension encourages better flowability of the material. It should be noted that extremely low melt viscosity compromises the surface roughness of the printed components because the melt seeps into the surrounding support powder [8]. Viscosity, surface tension and shear stress thus form crucial material-property requirements for PLS polymers.

3.4 Optical properties

Optical properties influence the PLS process. A suitable polymeric material should be able to absorb sufficient laser energy to ensure satisfactory fusion of the powder particles. Most of the polymers sufficiently absorb laser energy of the commonly utilized CO2 laser with a wavelength of about 10 μm [17]. The optical characteristics of most polymers are sufficient for PLS processing; therefore, they do not significantly affect PLS processing of polymers.

4 Findings and discussion: various techniques commonly used to characterize polymer powders used in PLS

There are various techniques for the characterization of polymers powders for PLS. These techniques are classified according to whether they address the intrinsic or extrinsic properties of powder. The ensuing discussion provides details of the commonly utilized strategies for the characterization of powder in these two categories.

4.1 Determination of powder density using gas pycnometry

Powder density is commonly determined using a gas pycnometry technique. A gas pycnometer is a device that uses a gas, such as nitrogen or helium, to determine the density of a particular material [24]. Helium gas is commonly utilized because it exhibits ideal gas characteristics. Various types of gas pycnometers include constant-volume pycnometers, variable-volume pycnometers, and comparative pycnometers [25]. The general procedure for using the equipment involves first weighing a sample of polymer powder. The sample is then placed into a pycnometry container of known volume. Helium is utilized to displace the air. The volume of helium used is obtained using the ideal gas law. Subtracting this volume from the volume of the container yields the volume of the particles of powder. The density of the powder is then determined using the following expression: Density = kg m 3 = Mass ( kg ) volume ( m 3 ) (1)

The gas pycnometry technique is associated with the advantages of ease of use, the machine can be left unattended after loading, guaranteed reproducibility and pycnometers are pre-calibrated and are therefore ready for use. However, the method is limited by operator-dependent reading which reduces accuracy.

4.2 Laser diffraction technique

The laser diffraction technique is employed in determining the distribution of powder particles using diffraction of a laser beam. During the process, a laser beam is allowed to pass in between particles and the angular distribution of scattered light is analyzed [17]. When the particles are suspended in a liquid, the process is referred to as wet laser diffraction, whereas when the particles are suspended in the air, the technique is termed as dry laser diffraction [17]. The technique makes use of the Fraunhofer and Mie theories. The Fraunhofer theory assumes that all the particles are much larger than the wavelength of the laser beam used. The particles should be at least 40 times the wavelength of the laser beam [26]. Hence, only scattering at the contour of the particles is considered. The Mie theory is used when the particles are much smaller than 40 times the wavelength of the laser beam [26]. The advantages of the laser diffraction technique include small quantities of samples required, short time of analysis, reliability, and reproducibility. However, high cost of instrumentation limits the use of the laser diffraction technique for characterization of powder [27].

4.3 Scanning electron microscopy

The Scanning Electron Microscope (SEM) technique can be used to determine the morphology of powder particles. A schematic representation of a SEM complete with its accessories is shown in Figure 4. The SEM operates by focusing a beam of electrons from an electron gun at a test specimen using a system of electromagnetic lenses [28]. Once the beam of electrons hits the specimen the secondary electrons, backscattered electrons, transmitted electrons or the current generated in the specimen are used to provide signals for SEM observations [29]. The magnification of a SEM is a function of the amount of current supplied [29].

Before testing, polymeric powders should be dried well. The powder is then plated with gold or platinum to reduce surface charging [29]. After this, the powder is mounted firmly inside the SEM and then tested, adhering to standard testing parameters (especially the accelerating voltage). An accelerating voltage of 25 kV is recommended for PLS polymeric materials [30]. Figure 5 shows an example of powder morphology obtained using SEM. The experiment giving rise to the micrographs was conducted by Berretta et al. [30] to determine the morphology of PA2200 powder.

The SEM technique offers various advantages: for example, it is easy to operate the equipment. In addition to this, SEM provides detailed images with versatile information [31]. It is also fast, taking less than five minutes to obtain results. The limitations of SEM include the size of sample scanned and cost of the equipment. The SEM also requires a large space. Besides, the preparation of specimens is time-consuming and special training is required to operate the equipment.

thumbnail Fig. 4

Schematic diagram of an SEM [28].

thumbnail Fig. 5

Powder morphology for virgin PA2200 using low (A), medium (B), and high magnifications (C) [30].

4.4 Differential scanning calorimetry

Differential Scanning Calorimetry (DSC) is a thermo-analytical strategy that is utilized when investigating the thermal properties of polymers. The technique is used to differentiate between appropriate and less suitable powders for use in PLS. The set-up of the DSC process is as shown in Figure 6.

During the DSC process, the samples of known mass are heated and cooled and the alterations in heat capacity of a particular material with respect to changes of heat flow are monitored. A typical DSC thermogram is represented in Figure 7.

The following parameters are obtained from a DSC test: onset of melting (Tm) and crystallization (Tc) points, peak melting and crystallization points, sintering window (TmTc), and degree of crystallization represented by the symbol (C%) defined as (ΔHm/ΔH0m) × 100% [13], where the symbol ΔHm stands for experimental melting enthalpy and ΔH0m stands for theoretical melting enthalpy of the material. The DSC is the second-most-used technique for characterization of PLS polymeric materials. The method is popular due to the short sample throughput, elaborate thermal properties and the small size of samples required. DSC is limited in that it is dependent on the skill of the operator. The technology is also very sensitive to changes, such as external temperature, which reduces the accuracy of the results obtained.

thumbnail Fig. 6

A DSC experimental set-up [32].

thumbnail Fig. 7

Typical example of a DSC thermogram [17].

4.5 Thermogravimetric analysis

Thermo gravimetric analysis (TGA) is a technique utilized to establish the degradation of a substance by monitoring the mass of the substance as a subject of temperature or time [33]. The apparatus consists of a pan, precision balance, temperature programmer, recorder and a furnace, as shown in Figure 8. During the experiment, the mass of a sample is monitored when heating or cooling. The exercise should be conducted in the presence of an inert gas such as helium or neon.

A typical TGA thermal curve is shown in Figure 9, from which the temperature at which the polymer degrades (Td) can be determined. The temperature of degradation is the point at which the curve of mass against temperature changes abruptly at the point of the intersection of the upper horizontal curve and the tangent of the sigmodal curve running through its point of inflexion.

The TGA technique requires small sample quantities with minimal preparation. The method is also highly accurate. However, it is not easy to interpret the data obtained.

thumbnail Fig. 8

Typical experimental set-up for thermogravimetric analysis [33].

thumbnail Fig. 9

An example of TGA thermal curve [34].

4.6 Melt flow index (MFI) testing

The melt flow index testing is conducted using an MFI tester for purposes of determining the ease of flow of a material. For polymers such as polyamide 12 and polypropylene, the tester consists of a 2.16 kg test load, charging rod, cleaning rod, tungsten carbide die with a capillary diameter of 2.095 mm, and a die ejector [35], as shown in Figure 10.

The testing process begins by cleaning the barrel and die using the cleaning tool and special cleaning paper. After cleaning, about six grams of the powder sample is loaded into the barrel. The piston with a mounted test load is inserted into the barrel and the powder in the barrel is preheated for about six minutes to different temperatures for different polymers; for instance, 230 °C for polypropylene and 235 °C for polyamide 12 [35]. The time taken by the piston to move between two marked points is measured. The mass of the ejected polymer material is determined using an electronic weighing machine and the value of MFI calculated using Equation (2). The MFI value of virgin PA12 is about 45–50 g/10 min and it degrades from this range with repeated use [36]. After the value reduces below 18 g/10 min, the powder is discarded, which happens after the 7th or 8th re-use cycle [37]. The cut-off points for other materials, such as PP, have not been determined experimentally. The MFI is the most commonly utilized characterization technique for PLS polymeric materials because it is easy to use, inexpensive, does not require specialized training and yields rheological properties of polymeric material which determines the suitability of the polymer being tested. However, it has limited accuracy and reproducibility. MFI = 600 Mass of polymer extruded Time taken to extrude the polymer (2)

thumbnail Fig. 10

A typical arrangement of an extrusion plastometer [35].

4.7 Gel permeation chromatography

Gel Permeation Chromatography (GPC) technology is used to determine the molecular weight of the powders. The method is a type of size exclusion chromatography technique (SEC) and involves separating the powder particles from the largest to the smallest [38]. The technique involves determining the molecular weight of the polymer based on retention time for penetration into a porous material. During testing, the samples are dissolved in a solvent such as 1,1,1,3,3,3-hexafluoro-2-propanol' (HFIP) (99.5%) and stirred for 24 h [38]. After this the samples are allowed to settle for 12 h. The samples must be filtered prior to the experiment. The injection volume should then be set as 20 µl and the flow rate as 0.700 ml/min. The GPC technique requires a short time for the preparation of samples. In addition, the actual measurements are simple, quick and reproducible. However, it is subject to inaccuracy.

4.8 The zero-shear test

The zero-shear test is performed on a rotational rheometer such as the one shown in Figure 11. Measurements are usually conducted between shear rates of 0.005 and 0.01 s−1 [39]. In zero-shear tests, powder tablets are commonly used to facilitate loading. These tablets are prepared using a plate press at a temperature and pressure of 80 bar and 100 bar, respectively [39].

The rotational rheometer is easy, fast and inexpensive to operate. Furthermore, small sample sizes are required. However, it does not yield sufficient data to accurately characterize polymeric materials.

thumbnail Fig. 11

Schematic representation of a rotational rheometer [40].

4.9 Determining the flowability of powder material using the Hausner number

Hausner ratio is a dimensionless number which is a quotient between the tapped density of a material and its bulk density [41]. Bulk density is the ratio of the mass of a polymeric material to the volume occupied by the material [41]. This value can be obtained using a bulk density tester. Tapped density is obtained by filling a specific measuring cylinder with polymeric powder material and then compacting the powder by knocking the cylinder on a board at a particular frequency [24]. The Hausner ratio determines the flowability of a material. The ratio is inversely proportional to the flowability of a material. Polymers with a Hausner number less than 1.25 show free-flowing behaviour, while polymers with a Hausner number greater than 1.4 have flowability problems [13,18]. The best flowability is obtained when the Hausner ratio is equal to one [13]. The Hausner number is obtained using Equation (3). Hausner Number = Tapped Density Bulk Density (3)

Hausner number testing is simple, inexpensive and does not require specialized testing. The technique is susceptible to inaccuracies and it does not yield sufficient data.

Flowability of powder can also be measured using other different techniques. Schmid et al. [42] summarized some of these methods as illustrated in Table 1.

The methods are easy to use and can substitute the MFI testing, which focuses only on the viscosity of melt material as opposed to the powder flowability.

Table 1

Common techniques for determining powder flowability [42].

4.10 Measuring the optical properties of PLS polymeric materials

The optical properties of polymers influence the rate at which they absorb laser energy. A suitable material should take sufficient laser energy to ensure satisfactory coalescence of the powder particles to prevent porosity which affects mechanical strengths of printed parts. Studies show that most polymers absorb sufficient laser energy at a wavelength of around 10 μm [17,19].The method used by Laumer et al. [43] to determine the optical properties of polymeric powders uses two spheres (Fig. 12). The set-up measures reflectance, transmittance, and absorbance of the powder material. The process commences by depositing a polymer material in a specimen holder which is positioned between the spheres. A potassium chloride specimen holder is used when using a CO2 laser beam (wavelength, 10.6 μm), while a soda-lime glass holder is utilized for a thulium fibre laser beam (wavelength, 1.94 μm). After setting up the apparatus, the laser beam propagates through the samples at an inclination of 8° from the upper sphere (see Fig. 12). The inclination prevents direct reflection of the beam through the opening of the upper sphere. At contact, the powder reflects the beam and the reflected power is measured by two heads on the spheres. The powder also absorbs and transmits the beam. The transmitted beam is measured in the same way as the reflected beam. After this, the absorbed beam is then calculated using computer software on the basis that the total power = reflected power + transmitted power + absorbed power. The optical characteristics of polymers are seldom investigated because most polymers absorb sufficient laser energy for PLS processing.

It is evident that the amount of energy absorbed by polymeric materials is subject to the reflection, transmission, and absorption properties. Hence, energy absorption capacity of materials might be influenced by their color. Translucent materials are expected to absorb laser energy more compared to white powder because of reduced reflection and transmission, which promotes energy absorption. Ligon et al. [44] proposes addition of graphite or carbon black if the absorption of a polymer is not sufficient.

thumbnail Fig. 12

Set-up for measuring optical properties of PLS polymeric materials [43].

5 Up-to-date investigations on the comparisons of properties between virgin and aged powder

As has been noted in this paper, PLS is a high-temperature process which degrades the properties of polymer feedstock materials, and thus affects recyclability. The material properties of the feedstock that are most altered by the high-temperature processes include particle size and distribution, rheological characteristics and thermal behaviour. The mechanical properties of the printed components are also impacted by the re-use of the powder. The ensuing discussion investigates the influence of re-use of common polymeric materials in the PLS process. PA12 accounts for 95% of all polymeric powders used in PLS, thus the preponderance reference to it here [5,8].

5.1 Effects of PLS re-use cycles on polymeric powder particle size and distribution

Dadbakhsh et al. [39] investigated the effects of PA 12 powder re-use on the properties of the powder. The authors considered virgin, aged, and aged-virgin mixture powder batches. A Malvern Master sizer Microplus that uses laser diffraction technology was employed to measure particle size distribution (PSD). It was established that the size of powder for the three batches remained around 55–60 μm, as illustrated in Figure 13. A summary of the particle sizes of the three batches of powder is shown in Table 2.

In another study, Ghita et al. [45] found that the mean size of polyether ketone (PEK) powder particles increased marginally when subjected to a high laser sintering process. Moreover, the particle size distribution was observed to widen after aging (Fig. 14). The authors noted that deviation from the optimal powder size introduces difficulties in processing due to problems of flowability of particles that were too small. Although flowability is subject to the properties of particles, such as size and morphology, it is also influenced by the environmental factors (humidity and temperature) [19,20]. Hence, PLS powders should be stored in a dry environment to prevent absorption of moisture, which in turn would affect the flowability and processability of the materials.

Research by Mwania et al. [46] on Laser PP CP 60, a polypropylene material from Diamond Plastics, GmbH, showed similar characteristics. In this work, the average powder particle size was seen to increases lightly after a single print cycle, as illustrated in Table 3.

thumbnail Fig. 13

Typical results obtained from the laser diffraction of polyamide 12 [39].

Table 2

Results from a laser diffraction test for PA [39].

thumbnail Fig. 14

Powder particle distribution for virgin and used HP3 PEK material [45].

Table 3

Particle size distribution for Laser PP CP 60 after print cycle [46].

5.2 Effects of PLS re-use cycles on rheological properties of polymeric powder

Dadbakhsh et al. [39] also found that molecular weight of powder increases with aging which is attributed to cross-linking of the long carbon chains. The authors measured the molecular weight of the powder using gel permeation chromatography. This claim is consistent with the findings of Rüsenberg et al. [47], as illustrated in Figure 15. The graphs in Figure 15 show that the used powder (red curve) has a higher molecular weight than the virgin material (blue curve).

It is expected that the viscosity of the PLS polymeric material should rise with increasing molecular weight after each re-use cycle. These expectations were confirmed by Gornet et al. [48], who measured the flow characteristics of PA 12 powder from 3D Systems Corporation using an extrusion plastometer. It was found in this work that the melt flow rate of the powder decreased with each build cycle, as shown in Figure 16.

Kuehnlein et al. [49] also established that the viscosity of PA 12 increases with processing time. The authors found that the melt flow rate of the material reduced from 28 cm3/10 min to 7 cm3/10 min after four hours of oven storage at 170 °C. Moreover, another study by Aldahsh [50] established that the viscosity of a cement/PA 12 composite increased with processing time and temperature. Wegner and Ünlü [51] showed that PP powder experiences minimum deterioration of rheological properties. They found that the MFI of PP material decreases only by 3% when the powder is re-used in the PLS process [51]. Figure 17 shows the trend of MFI changes of PP after two re-use cycles.

Increased viscosity also affects the properties of the printed parts. For PA 12 powder material, an “orange peel” surface texture is formed that adversely impacts the geometrical, dimensional accuracy and surface roughness of built components [39]. This demands that used PA 12 be mixed with virgin material after every cycle to prevent formation of the “orange peel”. The mixing ratio is proposed by the manufacturers, EOS GmbH Electro Optical Systems and 3D Systems Corporation, as 70:30 and 50:50 for aged to virgin powder ratio, respectively. EOS GmbH Electro Optical Systems manufactures PA 2200, while 3D Systems Corporation produces Duraform, PA 12 polymeric powder grades. The phenomenon of the formation of “orange peel” in other polymers, such as PP, due to re-use has not been examined extensively, but is attributed to increasing viscosity of the materials arising from increasing molecular weight. Hence, there is need for further investigation on the effects of PLS re-use cycles on the properties of polymeric powder materials.

Apart from viscosity, molecular weight of the materials affects the degree of crystallinity of the powder as well. Dadbakhsh et al. [39] determined that the crystallinity of PA 12 powder increases with aging to a maximum point after which it starts to decrease. The phenomenon can be attributed to the crystal growth during the PLS process which results in increased crystallinity. However, after the powder is melted, the higher molecular weight and long carbon chains prevent ordered chain folding resulting in reduced crystallinity. Increase in crystallinity increases the ultimate tensile strength of printed parts at the expense of percentage of elongation to break which decreases [8]. Besides, increased crystallinity increases curling and shrinkage rate of printed parts which affects the printing process of polymeric materials [8]. For a successful PLS process, the material should exhibit minimal curling to ensure free movement of the recoater, as the PLS process is terminated when the recoater picks up parts from the laser bed due to effects of curling.

Another study by Schmid et al. [42] analyzed the flowability of aged Duraform DF using Hausner Ratio. The authors used the round Robin test (DIN 38402-45), where it was established that the Hausner number of the powder increased from 1.148 to 1.225 after a single print cycle. The results indicate that the flowability of the materials decreases with printing cycles, which will impede recyclability. Suitable PLS materials should have a Hausner ratio less than 1.25. Polymeric powders with values greater than 1.4 are considered cohesive, and difficult to print.

thumbnail Fig. 15

The relationship between molecular weight of polyamide 12 and ageing [47].

thumbnail Fig. 16

The trend of melt flow rate of PA 12 powder with re-use cycles [48].

thumbnail Fig. 17

The trend of melt flow rate of PP powder with re-use cycles [51].

5.3 Effects of re-use PLS cycles on thermal properties of polymeric powder

The melting points of polymeric materials are also affected by the re-use of powder. Gornet et al. [48] utilized DSC to investigate the influence of re-using PA 12 powder on the melting point of the material. The authors found that the melting point increases with the number of build cycles, as illustrated in Figure 18. Higher melting points require larger pre-heating temperatures which increase chances of degradation of powder [8].

A study by Mwania et al. [46] illustrated that the sintering window of PP powder decreases after the first re-use cycle (Fig. 19). This phenomenon is attributed to degradation and cross-linking of the long carbon chains. A converse phenomenon was also observed by Dadbakhsh et al. [39] who investigated the effects of re-use cycles on the sintering window for PA 12 powder. The difference between the two materials might be ascribed to the differences in changes of the long carbon chains when subjected to high temperatures. Figure 20 shows that the gap between melting and crystallization points is wider for aged powder than that for virgin materials. The sintering window affects the cooling rate of printed parts. Materials with larger sintering windows exhibit even cooling rates. Hence, a larger sintering window decreases curling and shrinkages rates of printed parts.

thumbnail Fig. 18

Melting points of PA 12 with re-use cycles [48].

thumbnail Fig. 19

The sintering window of the PP virgin, used, and used-virgin mixture powders [46].

thumbnail Fig. 20

DSC thermogram for virgin, aged and mixed PA 12 powder [39].

5.4 Effects of PLS re-use cycles on the mechanical properties of parts printed using polymeric powder materials

Re-use of polymeric materials affects the mechanical properties of printed parts. Dadbakhsh et al. [39] found that ultimate tensile stress and elongation of PA 12 reduced after aging, but adding fresh materials ameliorates the properties, as illustrated in Table 4.

Another study by Wegner and Ünlü [51] found that mechanical properties of parts produced using PP powder decrease with the number of re-use cycles (Fig. 21). The magnitude of the mechanical factors is also significantly influenced by the energy density of the laser beam used. Thus, suitable process parameters should be utilized when printing polymeric materials.

Table 4

Tensile and elongation to break (%) for virgin, aged, and mixed PA 12 powder.

thumbnail Fig. 21

Effects of the number of re-use cycles on the mechanical properties of polypropylene powder [51].

6 Limitations of existing methods of characterizing powders and future works

MFI and DSC testing are the most commonly used techniques for quantifying the degradation of PLS polymeric powders. However, the two approaches yield limited information on the materials tested; hence, the need for more comprehensive and easier-to-use technologies for this purpose. In this regard, this paper considers previous work conducted by Amado et al. [5]. The authors introduced a new technology for characterization of powder (Revolution Powder Analyzer) that investigates the dynamic behaviour of powder. The aim of the technique was to replace the conventional methods with a more efficient powder characterization strategy. The equipment used in this method consists of a rotating drum manufactured from aluminium with an inner diameter of 50 mm and a width of 25 mm. The sides of the drum are covered with a transparent glass to allow capturing of the behaviour of powder using an image acquisition system. The drum can rotate at different speeds (0–200 rpm) when conducting experiments. At low speeds the machines records flowability while at high speeds it tests for fluidization properties. The technology can also capture images (morphology) and particle size and distribution of the powder particles. An image of this equipment set-up is shown in Figure 22. The authors of this study proposed that future advances in the characterization of powders should focus on developing simple and easy-to-use mechanisms that can determine a wide array of intrinsic and extrinsic properties of PLS polymers, since the traditional methods determine a limited set of characteristics.

thumbnail Fig. 22

The proposed powder testing technology by Amado et al. [5].

7 Conclusions

  • There is a need to characterize virgin as well as used PLS polymeric powders to establish their suitability before using or re-using, because it has been established that the PLS process affects the physical, rheological and thermal properties of the polymeric powders.

  • Polymer laser sinter recycling of PA 12 powder has been shown to affect the mechanical properties, surface finish and dimensional accuracy of PLS printed parts.

  • There are a number of methods currently in use to characterize polymer powders for PLS including differential scanning calorimetry (DSC), thermogravimetric analysis (TGA), laser diffraction analysis, gas pycnometry, scanning electron microscopy (SEM) and melt flow index (MFI) testing.

  • Amongst these methods, the melt flow index (MFI) and differential scanning calorimetry (DSC) are the most commonly utilized techniques.

  • However, these two methods do not yield sufficient data to fully quantify the degree of degradation of polymeric powder exposed to PLS. Hence, there is a need for more comprehensive and easier-to-use technologies that test a wider scope of parameters.

  • The need to develop new technologies capable of testing a wide array of intrinsic and extrinsic properties of powders is underscored.

Abbreviations

AM: Additive Manufacturing

PLS: Polymer Laser Sintering

PA 12: Polyamide 12 (Nylon)

PP: Polypropylene

DSC: Differential Scanning Calorimetry

TGA: Thermogravimetric Analysis

SEM: Scanning Electron Microscopy

MFI: Melt Flow 1ndex

GPC: Gel Permeation Chromatography

Td: Degradation Temperature

Tm: Onset of Melting Point

Tc: Onset of Crystallization Point

C%: Degree of Crystallization

ΔHm: Experimental Melting Enthalpy

ΔH0m: Literature Melting Enthalpy

Competing interests

The authors declare that they have no competing interests.

Funding

The review was supported by the Collaborative Program in Additive Manufacturing. (Contract No. CSIR-NLC-CPAM-15-MOA-CUT-01).

Author contribution statement

All the authors were involved in development and editing of the report. Besides, all authors read and approved the final manuscript.

Acknowledgments

The financial support from the South African Research Chairs Initiative of the Department of Science and Technology and National Research Foundation of South Africa (Grant No. 97994) and the Collaborative Program in Additive Manufacturing (Contract No. CSIR-NLC-CPAM-15-MOA-CUT-01) is gratefully acknowledged. Thanks also to the Centre of Rapid Prototyping and Manufacturing (CRPM) for technical support.

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Cite this article as: Fredrick Mulinge Mwania, Maina Maringa, Jacobus G. van der Walt, A review of the techniques used to characterize laser sintering of polymeric powders for use and re-use in additive manufacturing, Manufacturing Rev. 8, 14 (2021)

All Tables

Table 1

Common techniques for determining powder flowability [42].

Table 2

Results from a laser diffraction test for PA [39].

Table 3

Particle size distribution for Laser PP CP 60 after print cycle [46].

Table 4

Tensile and elongation to break (%) for virgin, aged, and mixed PA 12 powder.

All Figures

thumbnail Fig. 1

Percentage distribution of polymers applicable to the PLS process [1].

In the text
thumbnail Fig. 2

A schematic representation of an PLS machine (EOSINT P380 Machine).

In the text
thumbnail Fig. 3

The heating profile of polymeric material during PLS [3].

In the text
thumbnail Fig. 4

Schematic diagram of an SEM [28].

In the text
thumbnail Fig. 5

Powder morphology for virgin PA2200 using low (A), medium (B), and high magnifications (C) [30].

In the text
thumbnail Fig. 6

A DSC experimental set-up [32].

In the text
thumbnail Fig. 7

Typical example of a DSC thermogram [17].

In the text
thumbnail Fig. 8

Typical experimental set-up for thermogravimetric analysis [33].

In the text
thumbnail Fig. 9

An example of TGA thermal curve [34].

In the text
thumbnail Fig. 10

A typical arrangement of an extrusion plastometer [35].

In the text
thumbnail Fig. 11

Schematic representation of a rotational rheometer [40].

In the text
thumbnail Fig. 12

Set-up for measuring optical properties of PLS polymeric materials [43].

In the text
thumbnail Fig. 13

Typical results obtained from the laser diffraction of polyamide 12 [39].

In the text
thumbnail Fig. 14

Powder particle distribution for virgin and used HP3 PEK material [45].

In the text
thumbnail Fig. 15

The relationship between molecular weight of polyamide 12 and ageing [47].

In the text
thumbnail Fig. 16

The trend of melt flow rate of PA 12 powder with re-use cycles [48].

In the text
thumbnail Fig. 17

The trend of melt flow rate of PP powder with re-use cycles [51].

In the text
thumbnail Fig. 18

Melting points of PA 12 with re-use cycles [48].

In the text
thumbnail Fig. 19

The sintering window of the PP virgin, used, and used-virgin mixture powders [46].

In the text
thumbnail Fig. 20

DSC thermogram for virgin, aged and mixed PA 12 powder [39].

In the text
thumbnail Fig. 21

Effects of the number of re-use cycles on the mechanical properties of polypropylene powder [51].

In the text
thumbnail Fig. 22

The proposed powder testing technology by Amado et al. [5].

In the text

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