This application is directed, in general, to thermoset polymers and more specifically melt-processable forms of such polymers, methods of synthesis, and, using such polymers in fused filament fabrication printing and to printers adapted to facilitate such printing.
Fused filament fabrication (FFF) printing is an increasingly accessible, rapid, low cost form of additive manufacturing technology for 3-dimensional (3D) polymer printing. Often, however, the thermoplastic polymers that are used for FFF printed parts lack the same isotropic toughness and reliability of injection or compression molded parts due to the poor interlayer adhesion between printed filaments leading to poor mechanical properties in the printed parts. Efforts have been made to develop thermoset polymers, with their generally better thermal stability, chemical resistance and mechanical properties than thermoplastics, for FFF printing, including synthesizing cross-linked melt-processable forms of thermoset polymers. Such efforts, however, have produced thermoset polymers which lead to FFF printed products with significant mechanical anisotropy, e.g., direction-dependent mechanical properties, such as varying toughness losses when deformed against the printed filament grain.
Thus, there is a continuing need to develop new melt-processable forms of thermoset polymers that are suitable for FFF printing manufacturing technologies.
The present disclosure provides in one embodiment, a melt-processable thermoset polymer comprising monomers cross-linked together by furan-maleimide Diels Alder adduct covalent bonds. At least about 1 percent of the furan-maleimide Diels Alder adduct covalent bonds of the polymer are de-cross-linked by a retro Diels Alder reaction at a temperature in a range from about 90° C. and less than about 300° C.
Another embodiment of the disclosure is a method of synthesizing a melt-processable thermoset polymer, comprising cross-linking monomers together including forming furan-maleimide Diels Alder adduct covalent bonds. At least about 1 percent of the furan-maleimide Diels Alder adduct covalent bonds of the polymer are de-cross-linked by a retro Diels Alder reaction at temperature in a range from about 90° C. and less than about 300° C.
Another embodiment is a filament fabrication printer comprising a syringe extruder, a needle connected to an outlet of the syringe extruder and a heating coil wrapped around the syringe extruder. The heating coil is configured to heat a melt-processable thermoset polymer held in the syringe extruder to a temperature in a range from about 90° C. and less than about 300° C.
Still another embodiment of the disclosure is a method of fused filament fabrication printing. The method comprises loading a melt-processable thermoset polymer into a syringe extruder and forming a melt of the melt-processable thermoset polymer by heating the syringe extruder to a temperature in a range from about 90° C. and less than about 300° C. The method comprises extruding the melt through a needle connected to an outlet of the syringe extruder to deposit a printed thermoset polymer part onto a print bed.
For a more complete understanding of the present disclosure, reference is now made to the following detailed description taken in conjunction with the accompanying FIGS., in which:
Embodiments of the present disclosure benefit from the use of furan-maleimide Diels-Alder (fmDA) chemistry to synthesize melt-processable thermoset polymers showing low mechanical anisotropy in FFF printed polymer parts. The reversibility of the cross-links formed in such polymers, a type of dynamic covalent furan-maleimide Diels Alder bond, facilitates these thermoset polymers to be melt-processable at elevated temperatures (e.g., greater than 90° C. in some embodiments), similar to thermoplastic polymers. After the polymers are deposited onto a print bed, the de-cross-linked polymers start to crosslink via Diels-Alder reaction at lower temperatures (e.g., less than about 90° C. in some embodiments). The cross-links can form in all directions within the printed parts, including within and between the printed layers, resulting in improved homogeneity of cross-linking throughout the printed part. This, in turn, beneficially reduces the mechanical anisotropy in the printed parts.
It was surprising that the melt-processable thermoset polymers disclosed herein could be made suitable for FFF printing because the cross-links formed within a printed network of the thermoset polymers are not completely reversible at a given temperature, but rather are in equilibrium. Even though the equilibrium is increasingly driven towards the reactants from the Diels-Alder adducts at higher temperature, only about 20%-30% of fmDA linkages in some embodiments undergo retro-cycloaddition at temperatures suitable for FFF printing using commercial printers (e.g., less than about 300° C. in some embodiments). Moreover such higher temperatures increase the risk of promoting side reactions, such as aromatization of the DA adducts, ring-opening of furfuryl rings and homopolymerization of maleimides, causing the loss of reversibility of cross-links, as well as polymer degradation. Therefore, a balance had to be obtained between maximal disassociation and minimal degradation of the reactants. A new FFF printer and method of FFF printing to facilitate achieving this balance are disclosed herein.
The Diels-Alder reaction is a [4+2] cycloaddition between a dienophile and a diene. Some variants of the DA reaction are thermally reversible through a retro-DA reaction, which can occur at higher temperatures.
Polymers samples were synthesized according to one of the reaction schemes shown in
DSC was performed on a Mettler Toledo DSC-1. Sample size was limited between 8-10 mg. Samples were tested under nitrogen at 50 mL/min and at a heating rate of 10° K/min except the cooling cycle of 3F-2M was at 1° K/min to ensure complete Diels-Alder reaction during the slow cooling.
DMA was performed on a Mettler Toledo DMA 861e/SDTA. Samples were cut into rectangular prisms approximately 25 mm long, 3 mm wide and 1 mm wide. The sinusoidal mode of deformation for the DMA was tension, with a frequency of 1 Hz, 5 N force amplitude and 21 μm displacement amplitude. Samples were tested in air at a heating rate of 2° K/min. At least three samples were tested for each composition.
The Poly(FMA-co-EMA) polymer displayed limited reversibility of the Diels-Alder reaction in a solvent-free environment.
A thermoset polymer (3F-2M) was synthesized in accordance to the reaction scheme presented in
Tensile testing was conducted to failure, performed on a Lloyd LR5KPlus Universal Materials Testing Machine with a 100 N load cell. Dog-bone samples were punched out of the 3D printed sheets or compression molded sheets by Carver Press with an ASTM D638 Type V dog-bone die. Typically 10 specimens were prepared and tested for each sample. Dog-bones were held between Lloyd TG22 self-tightening roller grips within a Eurotherm Thermal Chamber. The strain was measured by a Lloyd Laserscan 200 non-contacting laser extensometer. Each test was done at room temperature (19° C.) at 50 mm/min, with a preload of 0.2 N. The toughness was determined as the integration of the area under the stress-strain curve.
Additional measurements were performed on additional samples of the thermoset polymer (3F-2M) as well as commercial samples of NinjaFlex® (NF) and SemiFlex™ (SF) both purchased from NinjaTek™ as filaments. The thermoset polymer (3F-2M) was printed on a modified 3Drag printer purchased from Futura Group. The print head was modified into a syringe type print head. Heating and cooling system were installed to facilitate controlled heating and cooling during the printing. NF and SF were printed on a Lulzbot TAZ 5 3D printer at 230° C. and 225° C. with the print bed at 40° C. and 95° C.
The modified 3Drag printer and process allowed for printing of thermoset polymer (3F-2M) as a solid rectangular prism having dimension of about 67 mm tall, about 60 mm wide and about 1.5 mm thick in about 12 to 14 minutes. In comparison, the printing of same-dimension samples of NF and SF using the Lulzbot TAZ 5 3D printer took more than twice as long.
Both neat and 3D printed samples of three materials were characterized with differential scanning calorimetry (DSC), dynamic mechanical analysis (DMA) and tensile testing (stress-strain curves).
The DSC curves shown in
The DMA curves of NinjaFlex®, SemiFlex™ and 3F-2M are described in
Tensile testing of dog-bone samples of FFF printed parts from NinjaFlex®, SemiFlex™ and the thermoset polymer (3F-2M) was done in the same manner as described in the context of
As illustrated in
As illustrated in
TABLE 1 presents a comparison of the toughness of Neat and FFF printable engineering materials, NinjaFlex® (NF), SemiFlex™ (SF), and literature values for polylactic acid (PLA) polymer (see J. R. Davidson, G. A. Appuhamillage, C. M. Thompson, W. Voit, R. A. Smaldone, ACS Appl. Mater. Interfaces 2016, 8, 16961-16966) and acrylonitrile butadiene styrene (ABS) polymer (see S. Shaffer, K. Yang, J. Vargas, M. A. Di Prima, W. Voit, Polymer 2014, 55, 5969-5979) to the thermoset polymer (3F-2M) synthesized as disclosed herein.
As illustrated in TABLE 1 and
With continuing reference to
The modified DARE printer 1700 was developed in response to the impractically of feeding and extruding pre-formed filaments of Diels-Alder synthesized thermoset polymers through commercial extruder print heads. For polymer filaments to be printed on commercial extruder print heads, they need to be able to melt fast enough so the polymer can be melted at the tip of the hot end while the filament above the hot end stays solid so as to be able to push the melt out of the extruder nozzle.
As noted elsewhere herein, the fmDA cross-link within the network are not completely reversed at a given temperature, but rather are in equilibrium. In some embodiments, this means that the de-cross-linking process (e.g., melting of the fmDA polymers) is slow. While the de-cross-linking process could be speed up by increasing the temperature, in some embodiments, only about 20%-30% of fmDA linkages undergo retro-cycloaddition, and, higher temperatures increase the risk of side reactions, such as aromatization of the DA adducts, ring-opening of furfuryl rings and homopolymerization of maleimides, causing the loss of reversibility of crosslinks, as well as polymer degradation.
Achieving a balance of maximal disassociation of the thermoset polymer and minimal degradation of the reactants was facilitated by replacing the commercial printer extruder head with the syringe-type print extruder head 1720 and adding the additional components disclosed above.
In some embodiments, a method of FFF printing using the melt-processable thermoset polymers synthesized as disclosed herein include loading the polymer into the syringe-type print extruder head 1720. The syringe-type print extruder head 1720 was heated to a desired melting temperature (e.g., about 90° C. in some embodiments) via the heating coil 1740 wrapped around a metal (e.g., aluminum) syringe sleeve 1770 that the syringe 1720 is held in. After the polymer in the syringe 1720 melts, a piston 1775 of the printer 1700 pushes down the piston 1780 of the syringe 1720 to deposit the polymer melt onto a print bed 1785 via the syringe needle 1760. In some embodiments, one or both of the cooling systems 1710, 1715 can be activated through the end of printing to facilitate the proper cooling of the printed part during the printing. In some embodiments, the printed part (see e.g.,
In some embodiments, a computer program (e.g., written on open-source software such as Repetier) can be used to facilitate controlling the temperature of the heating coil 1740, and, during the printing, control when the cooling system 1710 starts to cool and/or further control the fan cooling system 1715 to blow cooling air through the pipe and the duct then onto the printed part.
In some embodiments where lower crosslink density is desired, to facilitate crystal formation or to form elastomeric materials) is desired, then a melt-processable thermoset polymer may be formed with at least about 1 percent de-cross-linking. Consider embodiments using a tri functional and a di functional maleimide monomer reacting with a di functional monomer (e.g., Furan). Some of the crosslinks would be cleaved and some of the chains would be cleaved. In some such embodiments, if the amount of crosslinking (tri functional or higher) molecules is, e.g. less than about 10 percent, then the amount of the trifunctional crosslinks needed to break to form a melt-processable thermoset polymer may much less than the total number of crosslinking bonds in the system (e.g., at least about 1 percent decrosslinking). In some embodiments, e.g., using a di functional maleimide and a trifunctional furan, at least about 20% decrosslinking, may be required.
In some embodiments, cross-linking the monomers together (step 1910) includes a step 1920 of forming the furan-maleimide Diels Alder adduct covalent bond between a furan functionalized pendent group of the monomers in one polymer chain and a first maleimide functionalized group of a cross-linker having bismaleimide functionalized groups, and, forming the furan-maleimide Diels Alder adduct covalent bond between a furan functionalized pendent group of the monomers in another polymer chain and a second maleimide functionalized group of the cross-linker. For instance, as part of step 1920, the polymer chains having the monomers with the furan functionalized pendent groups is a Poly(Furfuryl MethAcrylate-co-Ethyl MethAcrylate) polymer and the cross-linker is Methylenedi-phenylene bismaleimide.
Alternatively, in some embodiments cross-linking the monomers together (step 1910) includes a step 1930 of mixing a monomer with a bi- tri- or tetra-furan functionalized pendant group with a bis- or tris-maleimide functionalized monomer. For example in various embodiments as part of step 1930, the bis- or tris-maleimide functionalized monomer is bismaleimido tricyclodecane or ICN-3M and the monomer with the bi- tri- or tetra-furan functionalized pendant group is TCMDA-2F, ICN-3F or PETTA-4F (see e.g.,
In some embodiments, e.g., prior to mixing step 1930, the method 1900 can further include a step 1940 of synthesizing the monomer with the tri-furan functionalized pendant group. As a non-limiting example synthesizing (step 1940) can include dissolving trimethylolpropane triacrylate in dichloromethane containing triethylene amine to form a solution, adding furfuryl mercaptan to the solution to form a mixture and drying the mixture to remove unreacted furfuryl mercaptan and yield a tri-furan functionalized trimethylolpropane triacrylate monomer. Based on this example one skilled in the pertinent art would understand how other monomers with multi-furan functionalized pendant groups (e.g., monomers with bi- or tetra-furan functionalized pendant groups) could be synthesized by procedures analogous to that described for step 1940.
The example method 2000 can comprise loading a melt-processable thermoset polymer into a syringe extruder (step 2010). For instance, the melt-processable thermoset polymer can include monomers cross-linked together by furan-maleimide Diels Alder adduct covalent bonds, wherein least about 1 percent, and in some embodiments at least about 20 percent and in some embodiments at least about 30 percent, and in some embodiments less than about 40 percent, of the furan-maleimide Diels Alder adduct covalent bonds of the polymer are de-cross-linked by a retro Diels Alder reaction in the temperature range.
The method 200 can further comprise forming a melt (step 2020) of the melt-processable thermoset polymer by heating the syringe extruder to a temperature in a range from about 90° C. and less than about 300° C. The method 2000 can also comprise extruding the melt through a needle connected to an outlet of the syringe extruder to deposit a printed thermoset polymer part onto a print bed (step 2030).
Some embodiments of the method 2000 can further include cooling the partially completed printed thermoset polymer part (step 2040), e.g., after the polymer melt is extruded the needle as part of step 2030.
Some embodiments of the method 2000 can further include post curing or annealing the completed printed thermoset polymer part (step 2050).
Those skilled in the pertinent arts to which this application relates will appreciate that other and further additions, deletions, substitutions and modifications may be made to the described embodiments.
This Application claims the benefit under 35 U.S.C. §119(e) of U.S. Provisional Patent Application No. 62/377,789 filed Aug. 22, 2016, which is incorporated herein by reference in its entirety as if fully set forth herein.
Number | Date | Country | |
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62377789 | Aug 2016 | US |