Polymeric materials for use in 3D printing processes
Patent Information
- Application Number
- JP2024516791
- Authority / Receiving Office
- JP · JP
- Patent Type
- Applications
- Current Assignee / Owner
- Priority Date
- 2021-10-14
- Filing Date
- 2022-10-13
- Publication Date
- 2025-10-06
AI Technical Summary
High strength polyethylene materials are difficult to use in 3D printing due to inherent shrinkage and poor adhesion, particularly in fused filament manufacturing (FFF) and fused particle manufacturing (FPF) processes, limiting their application in industrial applications requiring high strength, such as pipes for conveying fluids and gases.
A polymeric material comprising high density polyethylene (PE) with a density of at least 0.930 kg/m³ and crystallinity of at least 50%, combined with fibrous fillers and optional nucleating agents, is used in material extrusion-based 3D printing to achieve a minimum strength of 10 MPa, suitable for complex shapes.
The solution enables fast and cost-effective manufacturing of high-strength 3D articles without adversely affecting other material properties, ensuring good adhesion and reducing production costs.
Smart Images

Figure 2023062140000001
Abstract
Description
[Technical field]
[0001] The present invention relates to polymeric materials suitable for the production of three-dimensional articles by additive manufacturing techniques. In particular, the present invention relates to the use of polyethylene-based polymer blends in material extrusion-based 3D printing processes. [Background technology]
[0002] According to the ISO 52900-2015 standard, the term "additive manufacturing" refers to a technique for creating three-dimensional (3D) objects using successive layers of material. In an additive manufacturing process, material is deposited, applied, or solidified under computer control based on a digital model of the 3D object to be manufactured to create a 3D article. The digital model of the 3D article can be created, for example, by using CAD software or a 3D object scanner.
[0003] Additive manufacturing processes are also referred to using terms such as "generative manufacturing methods" or "3D printing". The term "3D printing" was originally used for the inkjet printing-based AM process created by the Massachusetts Institute of Technology (MIT) during the 1990s. Compared to conventional techniques, which are based on object creation by either molding / casting or removing / machining material from a raw object, additive manufacturing techniques follow a fundamentally different approach to manufacturing. In particular, it is possible to modify the design of each object without increasing production costs and offering tailor-made solutions for a wide range of products.
[0004] Generally, in additive manufacturing processes, 3D articles are produced using amorphous (e.g., liquids, powders, granules, pastes, etc.) and / or shape-neutral (e.g., bands, wires, filaments) materials that are subjected to chemical and / or physical processes (e.g., melting, polymerization, sintering, curing or hardening). The main categories of additive manufacturing techniques include VAT photopolymerization, material extrusion, material jetting, binder jetting, powder bed fusion, directed energy deposition, and sheet lamination techniques. Widely used additive manufacturing techniques based on material extrusion include Fused Filament Fabrication (FFF) and Fused Particle Fabrication (FPF).
[0005] In the Fused Filament Fabrication (FFF) process, also known as Fused Deposition Modeling (FDM), a 3D article is fabricated using a polymeric material in the form of a filament based on a digital model of the 3D article. In the FFF process, the polymeric filament is fed to a moving printer extrusion head, heated above its glass transition or melting temperature, and then deposited through a heated nozzle of the printer extrusion head in a continuous series of layers. After deposition, the layer of polymeric material solidifies and fuses with the previously deposited layer. Fused Particle Fabrication (FPF), also known as Fused Granule Fabrication (FGF), differs from the FFF process only in that the polymeric material is provided in the form of particles, such as granules or pellets, instead of filaments.
[0006] Commonly used thermoplastic materials for fused filament and fused particle manufacturing processes include acrylonitrile butadiene styrene (ABS), polylactic acid (PLA), polycarbonate (PC), and polyamides, among others. For example, published patent application EP 3 476 898 A1 discloses a thermoplastic polymer composition for use in 3D printing comprising at least 25% by weight of an amorphous polyamide, at least 5% by weight of a crystalline or semi-crystalline thermoplastic polymer, and optionally at least 1% by weight of a filler.
[0007] High density polyethylene (HDPE) is a commonly used material in many commercial applications due to its high strength and low cost. However, the use of HDPE as a material for 3D printing, especially in material extrusion 3D printing, is known to be notoriously difficult due to the inherent shrinkage of the polymer material upon cooling and its poor adhesion to building plates. As a result, HDPE is generally not a preferred material for 3D printing. However, some industrial applications, such as pipes used to carry potable water, wastewater, slurries, chemicals, hazardous waste, or compressed gases, require a minimum required strength (MRS) according to ISO / TR 9080 of at least 10 MPa. In these applications, only polyethylenes with particularly high strength, such as PE100, can be used. The high density and crystallinity of PE100 make it extremely difficult to use in 3D printing, mainly due to the high shrinkage of the material upon cooling.
[0008] The challenges of using high strength polyethylene in 3D printing can be mitigated at least to some extent by careful control of process parameters and by blending other polymers with the polyethylene material. Another published patent application WO 2020 / 028013 A1 discloses a fused filament fabrication (FFF) process that involves using a thermoplastic blend comprising high density polyethylene (HDPE) and a second polymer, where the weight ratio of the amount of high density polyethylene to the amount of the second thermoplastic polymer is in the range of 1.5:1 to 20:1. However, blending HDPE with a second polymer, such as low density polyethylene (LDPE), strongly affects the mechanical properties of the 3D printed article. Summary of the Invention [Problem to be solved by the invention]
[0009] There is therefore a need for high strength polyethylene-based materials that are suitable for use as 3D printing materials, in particular for 3D printers operating with Fused Filament Fabrication (FFF) or Fused Particle Fabrication (FPF) technologies. [Means for solving the problem]
[0010] It is an object of the present invention to provide a high strength polyethylene based material that is suitable for use in material extrusion based 3D printing techniques, in particular for providing three dimensional articles using Fused Filament Fabrication (FFF) or Fused Particle Fabrication (FPF) processes.
[0011] Surprisingly, it was found that this object can be achieved by the features of claim 1.
[0012] In particular, it has been found that the polymer material as defined in claim 1 enables the fast and cost-effective production of custom 3D articles of complex shapes using material extrusion-based 3D printing techniques, the 3D articles having a minimum strength (MRS) according to ISO / TR 9080 of at least 10 MPa.
[0013] One advantage of the polymeric material of the present invention is that it improves the suitability of a basic polyethylene-based material for 3D printing applications without adversely affecting other properties of the polymeric material, particularly the strength of the material. Furthermore, the additional components added to the basic polyethylene material do not significantly increase the overall cost of the polymeric material.
[0014] Further subject matter of the invention is defined in the further independent claims. Preferred embodiments are outlined throughout the description and the dependent claims. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0015] The subject of the present invention is the use of a polymeric material for the manufacture of a 3D object by an additive manufacturing process, said polymeric material comprising: a) at least 0.930 kg / m 3 At least one polyethylene PE having a density at 23 ° C., measured according to the EN ISO 1183-1: 2019 standard, of at least 50% by weight of crystallinity, measured according to the EN ISO 11357-3: 2018 standard, b) at least one solid filler F; c) optionally at least one nucleating agent N; Including, The at least one solid filler F is a fibrous filler having an average aspect ratio (length / diameter) on a volume basis of 3 to 60, preferably 4 to 50; It is use.
[0016] The abbreviation "3D" is used throughout this disclosure in place of the term "three dimensional."
[0017] The term "polymer" refers to a population of chemically uniform macromolecules produced by polyreaction (polymerization, polyaddition, polycondensation) of monomers of the same or different types, which macromolecules differ with respect to their degree of polymerization, molecular weight, and chain length. The term also encompasses derivatives of said population of macromolecules resulting from polyreactions, i.e. compounds obtained by reactions, such as addition or substitution, of functional groups in a given macromolecule, and which may be chemically uniform or chemically non-uniform.
[0018] The term "molecular weight" refers to the molar mass (g / mol) of a molecule or of a part of a molecule, also called a "moiety". The term "average molecular weight" refers to the number average molecular weight (M n ) or weight average molecular weight (M w Molecular weights may be measured by gel permeation chromatography (GPC) using polystyrene as standards, styrene-divinylbenzene gels of porosity 100 Angstroms, 1000 Angstroms and 10000 Angstroms as columns, and tetrahydrofuran as solvent at 35° C. or 1,2,4-trichlorobenzene as solvent at 160° C., depending on the molecule.
[0019] The term "softening point" refers to the temperature at which a compound softens to a rubber-like state or at which crystalline moieties within a compound melt. The softening point is preferably measured by ring and ball measurements performed according to the DIN EN 1238:2011 standard.
[0020] The term "melting temperature" or "melting point" refers to the temperature at which a material undergoes a transition from a solid to a liquid state. m ) is preferably determined by differential scanning calorimetry (DSC) according to the ISO 11357-3 standard using a heating rate of 2° C. / min. The measurement can be carried out using a Mettler Toledo DSC 3+ device, T m The value can be determined from the measured DSC curve with the aid of DSC software. If the measured DSC curve shows several peak temperatures, the first peak temperature coming from the lower temperature side in the thermogram is the melting temperature (T m ) is considered to be
[0021] The term "glass transition temperature" (T g ) refers to the temperature above which a polymer component becomes soft and pliable and below which it becomes hard and glassy. g ) is preferably determined by dynamic mechanical analysis (DMA) as the peak of the measured loss modulus (G") curve using an applied frequency of 1 Hz and a strain level of 0.1%.
[0022] The "amount or content of at least one component X" in a composition, for example the "amount of at least one thermoplastic polymer TP", refers to the sum of the individual amounts of all thermoplastic polymers TP contained in the composition. Furthermore, if the composition comprises 20% by weight of at least one thermoplastic polymer TP, the sum of the amounts of all thermoplastic polymers TP contained in the composition is equal to 20% by weight.
[0023] The term "normal room temperature" refers to a temperature of 23°C.
[0024] The polymeric material for use in additive manufacturing processes has a modulus of at least 0.930 kg / m 3 , preferably at least 0.935 kg / m 3 , more preferably at least 0.940 kg / m 3 , and even more preferably at least 0.950 kg / m3 The polymer comprises at least one polyethylene having a density at 23°C, measured according to the EN ISO 1183-1:2019 standard, of at least 50% by weight, preferably at least 60% by weight, more preferably at least 70% by weight, of crystallinity, measured according to the EN ISO 11357-3:2018 standard.
[0025] The crystallinity of polyethylene PE is determined by formula (I):
number
[0026] According to one or more embodiments, the additive manufacturing process is a fused filament manufacturing or fused particle manufacturing process.
[0027] In the Fused Filament Fabrication (FFF) process, a polymer filament is fed into a moving printer extrusion head and heated to its glass transition temperature (T g ) or melting temperature (T m ) and then deposited continuously as a series of layers through a heated nozzle of the printer extrusion head. After deposition, the layer of polymer material solidifies and fuses with the previously deposited layers. The printer extrusion head is moved under computer control to define the shape to be printed, based on control data calculated from a digital model of the 3D article.
[0028] Fused particle manufacturing (FPF), also known as fused granulation manufacturing (FGF), differs from the FFF process only in that the polymeric material is provided in the form of particles, such as granules or pellets, instead of filaments.
[0029] Suitable compounds for use as the at least one polyethylene PE include ethylene homopolymers and ethylene copolymers.
[0030] Preferably, the at least one polyethylene PE has a melt flow index (190°C / 2.16kg) measured according to the ISO 1133-1:2011 standard of at least 1 g / 10 min, more preferably at least 2.5 g / 10 min, even more preferably at least 3.5 g / 10 min. According to one or more embodiments, the at least one polyethylene PE has a melt flow index (190°C / 2.16kg) measured according to the ISO 1133-1:2011 standard of 1 to 50 g / 10 min, preferably 2 to 25 g / 10 min, more preferably 3 to 15 g / 10 min.
[0031] Preferably, the at least one polyethylene PE has a flexural modulus at 23°C, measured according to the ISO 178:2019 standard of at least 450 MPa, more preferably at least 550 MPa, even more preferably at least 650 MPa, and / or a melting temperature, determined by differential scanning calorimetry (DSC) according to the ISO 11357-3:2018 standard using a heating rate of 2°C / min of at least 105°C, more preferably at least 110°C, even more preferably at least 115°C.
[0032] According to one or more embodiments, the at least one polyethylene PE has a flexural modulus at 23°C, measured according to the ISO 178:2019 standard, of 400 to 1500 MPa, preferably 500 to 1350 MPa, more preferably 600 to 1250 MPa.
[0033] Preferably, the at least one polyethylene PE represents at least 50% by weight, more preferably at least 65% by weight, even more preferably at least 75% by weight of the total weight of the polymeric material. In general, the expression "component X represents Y% by weight of the total weight of the composition" is understood to mean that the amount of component X constitutes Y% by weight of the total weight of the composition, i.e. the composition comprises Y% by weight of component X. According to one or more embodiments, the at least one polyethylene PE represents 55-97.5% by weight, preferably 65-97.5% by weight, more preferably 75-96.5% by weight of the total weight of the polymeric material.
[0034] According to one or more embodiments, the at least one polyethylene PE accounts for at least 75% by weight, preferably at least 85% by weight, more preferably at least 90% by weight, even more preferably at least 92.5% by weight, even more preferably at least 95% by weight, and most preferably at least 97.5% by weight of the polymeric base material of the polymeric material. The "polymeric base material" of the polymeric material is understood to include all polymeric compounds of the polymeric composition, including the at least one polyethylene PE.
[0035] The polymeric material further comprises at least a solid filler F which is a fibrous filler having an average aspect ratio on a volume basis of 3-60, preferably 4-50, more preferably 4-35, even more preferably 5-25.
[0036] The term "fibrous fillers" as used herein refers to fibers as well as acicular fillers, also known as whiskers, which typically have fiber lengths of less than 100 μm.
[0037] The term "aspect ratio" of a particle, as used herein, refers to the value obtained by dividing the length (L) of the particle by the diameter (D). "Length of a particle," as used herein, refers to the maximum Feret diameter (X) from a measured set of Feret diameters. Fe,最大), i.e., the longest Feret diameter. The term "Feret diameter" refers to the distance between two tangents on opposite sides of a particle parallel to a fixed direction and perpendicular to the direction of measurement. "Particle diameter" refers in this disclosure to the smallest Feret diameter (X Fe,最小 ), i.e., the shortest Feret diameter. Therefore, the aspect ratio is X Fe,最大 and X Fe,最小 It can be calculated as the ratio of
[0038] The aspect ratio of a particle can be determined by measuring the length and diameter of the particle using any suitable measurement technique, such as by using a dynamic image analysis method performed according to the ISO 13322-2:2006 standard, and calculating the aspect ratio from the measured dimensions of the particle as described above. The size of the particle is preferably measured in a dry dispersion method, in which the particles are dispersed in air, preferably by using a pneumatic dispersion method. The measurement can be performed using any type of dynamic image analysis device, such as a Camsizer XT device (trademark of Retsch Technology GmbH).
[0039] The term "volume-based average aspect ratio" in this disclosure refers to the aspect ratio below which 50% of all particles by volume have an aspect ratio less than the average aspect ratio value.
[0040] According to one or more embodiments, the at least one solid filler F has a volume-based average particle size D of 50 μm or less, preferably 35 μm or less, more preferably 25 μm or less. 50 and / or a volume-based average particle length L of at least 5 μm, preferably at least 10 μm, more preferably at least 15 μm, and even more preferably at least 20 μm. 50 has.
[0041] The term "volume-based mean diameter D 50 " means in this disclosure that 50% of all particles by volume have an average diameter D 50 Similarly, the term "volume-based average length L" refers to a diameter less than the value of50 " means that 50% of all particles by volume have an average length L 50 It refers to a length less than the value of.
[0042] According to one or more embodiments, the at least one solid filler F has a volume-based average particle size D of 1 to 100 μm, preferably 2.5 to 50 μm, more preferably 2.5 to 35 μm, even more preferably 2.5 to 30 μm, even more preferably 2.5 to 25 μm. 50 and / or a volume-based average particle length L of 10 to 1000 μm, preferably 15 to 500 μm, more preferably 20 to 350 μm, even more preferably 25 to 250 μm, and even more preferably 30 to 200 μm. 50 has.
[0043] The at least one solid filler F is preferably an inorganic filler.
[0044] Suitable inorganic fillers for use as the at least one solid filler F include, for example, glass fibers, aramid fibers, carbon fibers, silicon carbide fibers, alumina fibers, steel fibers, acicular wollastonite, and magnesium oxysulfate whiskers.
[0045] Preferably, at least one solid filler F has a water solubility of less than 0.1 g / 100 g water, more preferably less than 0.05 g / 100 g water, even more preferably less than 0.01 g / 100 g water at a temperature of 20° C. The solubility of a compound in water can be measured as the saturation concentration, where the addition of more compound does not increase the concentration of the solution, i.e., excess material begins to precipitate. Measurements of the water solubility of a compound in water can be performed using the standard "shake flask" method as defined in OECD Test Guideline 105 (adopted on July 27, 1995).
[0046] According to one or more embodiments, the at least one solid filler F is selected from the group consisting of glass fibers, carbon fibers, aramid fibers, silicon carbide fibers, alumina fibers, and acicular wollastonite, preferably from the group consisting of glass fibers and acicular wollastonite.
[0047] Preferably, the at least one solid filler F represents at least 0.5% by weight, preferably at least 1.0% by weight, more preferably at least 1.5% by weight, even more preferably at least 2.5% by weight of the total weight of the polymeric material.
[0048] According to one or more embodiments, the at least one solid filler F represents 5-35% by weight, preferably 10-30% by weight, more preferably 10-25% by weight, even more preferably 10-20% by weight of the total weight of the polymeric material.
[0049] According to one or more embodiments, the polymeric material further comprises at least one nucleating agent N.
[0050] Suitable compounds for use as the at least one nucleating agent N include nanoscale inorganic fillers, such as, for example, nanoscale calcium carbonate, titanium dioxide, barium sulfate, silicon dioxide, expanded graphite, multi-walled carbon nanotubes, montmorillonite clay, vermiculite, nanocomposite minerals, and talc. The term "nanoscale" is used in the present disclosure to refer to an average particle size d of 1 μm or less, preferably 500 nm or less, more preferably 250 nm or less. 50 It refers to a solid filler having the structure
[0051] The term "particle size" refers in this disclosure to the area-equivalent spherical diameter (X 面積 The term "average particle size d 50 " means that 50% of all particles by volume are d 50The particle size distribution can be determined by sieve analysis according to the method described in ASTM C136 / C136M-2014 ("Standard Test Method for Sieve Analysis of Fine and Coarse Aggregates").
[0052] Further compounds suitable for us as the at least one nucleating agent N include organic additives such as sisal fibers, 1,2-cyclohexanedicarboxylic acid, calcium salts, anthracene, potassium hydrogen phthalate, benzoic acid and its derivatives, and sodium benzoate and its derivatives.
[0053] According to one or more embodiments, the at least one nucleating agent N is selected from the group consisting of nanoscale calcium carbonate, titanium dioxide, barium sulfate, silicon dioxide, expanded graphite, montmorillonite clay, talc, multi-walled carbon nanotubes, vermiculite, nanocomposite minerals, 1,2-cyclohexanedicarboxylic acid, calcium salts, anthracene, potassium hydrogen phthalate, benzoic acid and its derivatives, and sodium benzoate and its derivatives.
[0054] Suitable nucleating agents are commercially available, for example, from Milliken under the trade name UltraGuard® Solution.
[0055] According to one or more embodiments, the at least one nucleating agent N represents 0.1 to 10 wt.-%, preferably 0.5 to 7.5 wt.-%, more preferably 1.5 to 5 wt.-%, even more preferably 2.5 to 5 wt.-% of the total weight of the polymeric material.
[0056] According to one or more embodiments, the polymeric material further comprises at least one color pigment CP, preferably selected from the group consisting of titanium dioxide, zinc oxide, zinc sulfide, barium sulfate, iron oxide, mixed metal iron oxides, aluminum powder, and graphite.
[0057] Although some of the compounds used in the present invention are characterized as being useful for specific functions, it should be understood that the use of these compounds is not limited to their typical functions. For example, at least one color pigment CP can also function as a nucleating agent for the polymeric component of the polymeric material.
[0058] Preferably, the at least one color pigment CP has an average particle size d of less than 1000 nm, more preferably less than 750 μm, even more preferably less than 500 nm. 50 has.
[0059] According to one or more embodiments, the at least one color pigment CP has a median particle size in the range of 50-1000 nm, preferably 75-750 nm, more preferably 100-650 nm, even more preferably 125-500 μm, even more preferably 150-350 μm, and most preferably 200-300 nm.
[0060] The polymeric material may further comprise one or more UV stabilizers, preferably at least one hindered amine light stabilizer (HALS).These types of compounds are typically added to polymer blends to prevent light-induced polymer degradation.Such UV stabilizers are especially required when the 3D article is used in outdoor applications.
[0061] Suitable hindered amine light stabilizers (HALS) include, for example, bis(2,2,6,6-tetramethylpiperidyl)-sebacate; bis-5(1,2,2,6,6-pentamethylpiperidyl)-sebacate; n-butyl-3,5-di-tert-butyl-4-hydroxybenzylmalonic acid bis(1,2,2,6,6-pentamethylpiperidyl)ester; 1-hydroxyethyl-2,2,6,6-tetramethyl-4-hydroxy-piperidyl; Condensation products of N,N'-(2,2,6,6-tetramethylpiperidyl)-hexamethylenediamine and 4-tert-octylamino-2,6-dichloro-1,3,5-s-triazine; tris-(2,2,6,6-tetramethylpiperidyl)-nitrilotriacetate; tetrakis-(2,2,6,6-tetramethyl-4-piperidyl)-1,2,3,4-butanetetraarbonic acid; and 1,1'(1,2-ethanediyl)-bis-(3,3,5,5-tetramethylpiperazinone).
[0062] Suitable hindered amine light stabilizers are commercially available, for example, under the Tinuvin® trade name (from Ciba Specialty Chemicals), such as Tinuvin® 371, Tinuvin® 622, and Tinuvin® 770; under the Chimassorb® trade name (from Ciba Specialty Chemicals), such as Chimassorb® 119, Chimassorb® 944, Chimassorb® 2020; and under the Cyasorb® trade name (from Cytec Industries), such as Cyasorb® UV 3346, Cyasorb® UV 3529, Cyasorb® UV 4801, and Cyasorb® UV 4802; and under the Hostavin® trade name (from Clariant), such as Hostavin N30.
[0063] The polymeric material may contain various further additives such as heat stabilizers, UV absorbers, antioxidants, plasticizers, dyes, matting agents, antistatic agents, impact modifiers, biocides, and processing aids such as lubricants, slip agents, antiblocking agents, and denest aids, etc. The total amount of these types of further additives is preferably 15% by weight or less, more preferably 10% by weight or less, and even more preferably 5% by weight or less, based on the total weight of the polymeric material.
[0064] Another subject of the invention is a method for producing a 3D object, comprising the following steps: i) providing a digital model of a 3D article; ii) printing the polymeric material of the present invention as described above based on the digital model using a 3D printer to form a 3D article. The method includes:
[0065] The 3D printer is preferably a fused filament fabrication or fused particle fabrication printer.
[0066] "Digital model" refers to a digital representation of a real-world object, for example a pipe fitting part, that accurately reproduces the shape of the object. Typically, the digital model is stored in a computer-readable data storage device, particularly a data file. The data file format can be, for example, a computer-aided design (CAD) file format or a G-code (also called RS-274) file format.
[0067] According to one or more embodiments, step ii) comprises: ii) providing a polymeric material to a 3D printer; ii2) heating the polymeric material to provide a molten polymeric material; ii3) depositing molten polymer material by using a printer extrusion head of a 3D printer in a selected pattern according to a digital model of the 3D article to form the 3D article. Includes.
[0068] In step ii2) of the process, the polymeric material is preferably heated to a temperature above the melting point of at least one polyethylene PE to obtain a molten polymeric material. If the polymeric material comprises multiple different polyethylenes with different melting points, the polymeric material is preferably heated to a temperature above the melting point of the polyethylene with the highest melting point.
[0069] The movement of the printer extrusion head in step ii3) of the method is controlled according to control data calculated based on a digital model of the 3D article. The digital model of the 3D article is preferably first converted into an STL file to tessellate the 3D shape of the article and slice it into digital layers. The STL file is transferred to the 3D printer using custom machine software. A control system, such as a computer-aided manufacturing (CAM) software package, is used to generate the control data based on the STL file. The control system can be part of the 3D printer or it can be part of a separate data processing device, such as a computer system.
[0070] The digital model of the 3D object is preferably obtained by 3D scanning of the 3D object. 3D scanning is a process of analyzing a real-world object, such as a pipe joint, to collect data about its shape. The collected data can then be used to build a digital model of the object. A control system can thereby be used to generate the digital model from the collected data. The control system can be part of the 3D scanner, or it can be part of a separate data processing device, such as a computer system. However, it is also possible to obtain a digital model by measuring all the lengths and angles of the 3D object by hand and manually generating the digital model using modeling software. Nevertheless, this is more time-consuming and error-prone than 3D scanning.
[0071] There are many different 3D scanners available on the market that can be used for 3D scanning. Scanning of 3D objects is done with handheld and / or portable 3D scanners. Handheld and / or portable 3D scanners do not require complex installations and allow for quick and easy scanning of 3D articles to be manufactured.
[0072] Preferably, the 3D scanner is designed for capturing objects with a length between 1 cm and 20 m, especially between 20 cm and 10 m.
[0073] In particular, the 3D scanner is a non-contact 3D scanner. Such kind of scanner emits some kind of radiation, for example light, ultrasound or x-rays, and detects its reflection by or passage through the object being scanned in order to probe the object.
[0074] For example, the 3D scanner is a scanner of the type “calibry 3d scanner” by the company Thor3d, Varshavskoe Sh.33, Moscow, Russia.
[0075] A further subject of the invention is a 3D article obtained by an additive manufacturing process using the polymer material of the invention.
[0076] The additive manufacturing process is preferably a fused filament manufacturing or a fused particle manufacturing process.
[0077] According to one or more embodiments, the article is a pipe or a pipe fitting. EXAMPLES
[0078] The raw materials shown in Table 1 were used in this example.
[0079] [Table 1]
[0080] Pellet production Pellets for the fused particle fabrication (FPF) process were prepared according to the following procedure.
[0081] A portion of the raw materials of the polymer composition were premixed in a tumbler mixer and then fed to a ZSK laboratory twin screw extruder (L / D 44) by a gravimetric dosing scale. Another portion of the raw materials was fed directly to the laboratory extruder by a gravimetric dosing trolley. The raw materials were mixed, dispersed, homogenized and discharged through the holes of the perforated extruder nozzle. The extruded strands were cooled using a water bath and cut into pellets of suitable size. The pellets were then dried in an oven to remove residual moisture.
[0082] 3D printing properties of polymer compositions The suitability of the polymer composition prepared above for 3D printing was tested by using the pellets as feed material in a fused particle manufacturing process.
[0083] 3D articles with a hollow cubic shape consisting of four outer walls with dimensions of 200 mm x 200 mm were fabricated from the test polymer materials using a Yizumi SpaceA 3D printer. Each 3D printed article consisted of 222 layers.
[0084] 3D printing was performed using the process parameters shown in Table 2 below.
[0085] [Table 2]
[0086] The suitability of each tested polymer composition for use as a feed material for 3D printing was estimated based on the properties of the 3D printed articles in terms of "warp degree" and tensile strength.
[0087] The components of the tested polymer compositions and the properties of the 3D printed articles are shown in Table 3.
[0088] Degree of warping The degree of warping was considered to be expressed by the radius of curvature (R) of the vertical walls of the 3D printed article (hollow cube). The radius of curvature (R) was determined for each 3D printed article using the following formula:
number
number
[0089] Tensile strength The tensile strength of the 3D printed articles was measured according to the EN 527-1B / 5 / 100 standard using dumbbell-shaped samples cut from the walls of the 3D printed articles in the horizontal (x, length) and vertical (z, interlayer) directions as shown in the figure below. The values for tensile strength shown in Table 3 were obtained as the average of three measurements made using samples cut from the same 3D printed article.
number
[0090] [Table 3]
Claims
1. 1. Use of a polymeric material for the production of a 3D article by an additive manufacturing process, said polymeric material comprising: a) at least one polyethylene PE having a density at 23 ° C, measured according to the EN ISO 1183-1:2019 standard, of at least 0.930 kg / m 3 and a crystallinity, measured according to the EN ISO 11357-3:2018 standard, of at least 50% by weight; b) at least one solid filler F; c) optionally at least one nucleating agent N; Including, the at least one solid filler F is a fibrous filler having an average aspect ratio (length / diameter) on a volume basis of 3 to 60, preferably 4 to 50; use.
2. 2. The use according to claim 1, wherein the additive manufacturing process is a fused filament manufacturing process or a fused particle manufacturing process.
3. 3. Use according to claim 1 or 2, wherein the at least one polyethylene PE has a melt flow index (190°C / 2.16 kg), measured according to the ISO 1133-1:2011 standard, of at least 1 g / 10 min, preferably at least 2.5 g / 10 min.
4. 3. Use according to claim 1 or 2, wherein the at least one polyethylene PE has a flexural modulus at 23°C, measured according to the ISO 178:2019 standard, of at least 450 MPa, preferably at least 550 MPa, and / or a melting temperature, determined by differential scanning calorimetry (DSC) according to the ISO 11357-3:2018 standard, using a heating rate of 2°C / min of at least 100°C, preferably at least 105°C.
5. 3. Use according to claim 1 or 2, wherein said at least one polyethylene PE constitutes at least 50% by weight, preferably at least 75% by weight, of the total weight of said polymeric material.
6. The at least one solid filler F has a volume-based average particle size D of 50 μm or less, preferably 35 μm or less. 50 and / or a volume-based average particle length L of at least 5 μm, preferably at least 10 μm 50 3. The use according to claim 1 or 2, wherein
7. 3. Use according to claim 1 or 2, wherein the at least one solid filler F is selected from the group consisting of glass fibres, carbon fibres, aramid fibres, silicon carbide fibres, alumina fibres and acicular wollastonite, preferably from the group consisting of glass fibres and acicular wollastonite.
8. Use according to claim 1 or 2, wherein said at least one solid filler F constitutes from 5 to 35% by weight, preferably from 10 to 25% by weight, of the total weight of said polymeric material.
9. 3. The use according to claim 1 or 2, wherein the at least one nucleating agent N is selected from the group consisting of nanoscale calcium carbonate, titanium dioxide, barium sulfate, silicon dioxide, expanded graphite, montmorillonite clay, talc, multi-walled carbon nanotubes, vermiculite, nanocomposite minerals, 1,2-cyclohexanedicarboxylic acid, calcium salts, anthracene, potassium hydrogen phthalate, benzoic acid and derivatives thereof, and sodium benzoate and derivatives thereof.
10. Use according to claim 1 or 2, wherein said at least one nucleating agent N constitutes 0.1 to 10% by weight, preferably 1.5 to 5% by weight, of the total weight of said polymeric material.
11. 1. A method for manufacturing a 3D article, comprising the steps of: i) providing a digital model of said 3D article; ii) printing the polymer material defined in claim 1 or 2 based on said digital model using a 3D printer to form said 3D article. A method comprising:
12. 12. The method of claim 11, wherein the 3D printer is a fused filament fabrication or fused particle fabrication printer.
13. A 3D article obtained by an additive manufacturing process using a polymer material as defined in claim 1 or 2.
14. 14. The 3D article of claim 13, wherein the additive manufacturing process is a fused filament manufacturing or fused particle manufacturing process.
15. 14. The 3D article of claim 13, wherein the article is a pipe or a pipe fitting.