The present invention relates generally to the field of block copolymer chemistry. More particularly, the present disclosure relates to the 3D printing of an ultrasoft, stretchable elastomer comprised of segments of bottle-brush based triblock copolymers. These elastomers are thermostable within a wide temperature range, and exhibit significant extensibility and softness as compared to plastics and other 3D printable elastomers.
Additive manufacturing, or 3D printing, produces customized objects by combining computer-aided design with 3D printing techniques, and can create multi-length scale structures inaccessible by conventional molding.[1-3] Yet existing feedstock for 3D printing is nearly all plastics, such as photocurable resins, thermoplastics, and thermosets.[2,4,5] All these materials are not only stiff with Young's moduli of 108-1010 Pa, but also fragile with typical extensibility below 10%.[5] By contrast, elastomers are much softer and more deformable. Thus, it has been innovated in both technology[6-8] and materials development[9-11] to 3D print elastomers, based on which are created functional structures and devices such as tissue scaffolds,[12,13] sensors,[14] actuators,[15,16] and soft robots.[8,17] The basic materials, however, are limited to thermo-reversible liquid crystal elastomers and a few photo- or thermo-curable elastomers.[15,18-20] Although the moduli of these elastomers, 106-108 Pa, are much lower than that of plastics, they remain orders of magnitude higher than that of ultrasoft biological tissues, 102-105 Pa.[21] The further lowering of the stiffness of elastomers to this resulting range may significantly broaden their applications. One example is hydrogels.[22-24] However, hydrogels contain a large amount of water that can evaporate or leach out, and in doing so material properties will deteriorate. It remains a challenge to develop 3D printable, ultrasoft, yet solvent-free elastomers.
There is therefore a need in the art for an effective 3D printable, ultrasoft, and solvent-free elastomer.
The present inventor seeks to overcome this challenge by exploiting the self-assembly of a responsive ABA triblock copolymer, in which the A blocks are a linear polymer of relatively high glass transition temperature Tg, whereas the B block is a bottlebrush polymer with a linear backbone densely grafted by low Tg linear polymers (
More specifically, the present invention provides, among other things, 3D printable, ultrasoft, stretchable elastomers that are developed by exploiting the self-assembly of responsive bottlebrush-based triblock copolymers. The microphase separation of the architecturally and chemically distinct blocks results in physically crosslinked networks that are stimuli-reversible, enabling their use for direct-write printing deformable 3D structures. The elastomer claimed herein exhibits an extensibility up to 600% and a Young's modulus minimum of ˜102 Pa. This is 100 times softer than all existing 3D printable elastomers.
Other embodiments of the present invention include among other things, an ultrasoft, stretchable, reversible elastomers for direct-write printing deformable structures, as well as soft elastomers for additive manufacturing.
Existing feedstock for additive manufacturing, or 3D printing, are nearly all plastics, which are not only stiff with elastic moduli above 108 Pa but also fragile with breaking strain below 10%. An aspect of an embodiment of the present invention provides, among other things, the design and fabrication of a new class of thermo-reversible soft elastomers for additive manufacturing. Unlike conventional stiff, fragile plastics, these elastomers are soft with elastic moduli in the range of 1 kPa-100 kPa and extensible with breaking strain >100%. Moreover, these materials are solid at room temperature, but become liquid at high temperature. Such a temperature triggered solid-to-liquid transition allows the elastomers amenable extrusion-based 3D printing. Using temperature triggered direct-ink-writing, we create a complex, hierarchical 3D structure with an exceptional combination of softness and deformability that are inaccessible by conventional 3D printable polymers.
The polymer network formed by the self-assembly of the triblock copolymers (
An aspect of an embodiment of the present invention provides, among other things, a triblock copolymer comprising: a linear polymer wherein the linear polymer creates glassy domains within the triblock copolymer, and a bottlebrush polymer, wherein the bottlebrush polymer connects the glassy domains.
An aspect of an embodiment of the present invention provides, among other things, a triblock copolymer comprising: a linear polymer, wherein the linear polymer is poly(benzyl methacrylate); and a bottlebrush polymer, wherein the bottlebrush polymer is comprised of polydimethylsiloxane side chains, wherein the bottlebrush polymer is situated between two of the linear polymers.
An aspect of an embodiment of the present invention provides, among other things, a method of making a triblock copolymer, comprising: synthesizing a bottlebrush polymer; and adding one or more of the linear polymer to the bottlebrush polymer to yield the triblock copolymer.
An aspect of an embodiment of the present invention provides, among other things, a polymer network comprising a plurality of triblock copolymers, wherein: the bottlebrush polymers configured to operate as elastic network strands; and the linear polymers aggregate to form spherical glassy domains.
An aspect of an embodiment of the present invention provides, among other things, a method for 3D printing an elastomer, comprising: adding a solvent to polymer network at a specified pressure in a chamber of a 3D printer apparatus; transferring the polymer network with the solvent from a printer nozzle of the 3D printer apparatus; and wherein the solvent evaporates after exiting the nozzle and the glassy domains of the polymer network reassociate.
An aspect of an embodiment of the present invention system and method provides, among other things, a class of 3D printable, ultrasoft and stretchable elastomers by exploiting the self-assembly of responsive bottlebrush-based triblock copolymers. The microphase separation of the architecturally and chemically distinct blocks results in physically crosslinked networks that are stimuli-reversible, enabling their use for in-situ direct-write printing soft, elastic, and deformable 3D structures. The elastomers are 100% solvent-reprocessable yet thermostable within a wide range of temperature. Moreover, they exhibit an extensibility up to 600% and a Young's modulus low to ˜102 Pa, 10 times softer than plastics and more than 100 times softer than all existing 3D printable elastomers.
Although example embodiments of the present disclosure are explained in some instances in detail herein, it is to be understood that other embodiments are contemplated. Accordingly, it is not intended that the present disclosure be limited in its scope to the details of construction and arrangement of components set forth in the following description or illustrated in the drawings. The present disclosure is capable of other embodiments and of being practiced or carried out in various ways.
It should be appreciated that any of the compositions referred to with regards to any of the present invention embodiments discussed herein, may be integrally or separately formed with one another. Moreover, various compositions may be substituted with other modules or components that provide similar functions.
It should be appreciated that the device and related components discussed herein may take on all shapes along the entire continual geometric spectrum of manipulation of x, y and z planes to provide and meet the environmental, anatomical, and structural demands and operational requirements. Moreover, locations and alignments of the various components may vary as desired or required.
It should be appreciated that various sizes, dimensions, contours, rigidity, shapes, flexibility and materials of any of the components or portions of components in the various embodiments discussed throughout may be varied and utilized as desired or required.
It should be appreciated that while some dimensions are provided on the aforementioned figures, the device may constitute various sizes, dimensions, contours, rigidity, shapes, flexibility and materials as it pertains to the components or portions of components of the device, and therefore may be varied and utilized as desired or required.
It must also be noted that, as used in the specification and the appended claims, the singular forms “a,” “an” and “the” include plural referents unless the context clearly dictates otherwise. Ranges may be expressed herein as from “about” or “approximately” one particular value and/or to “about” or “approximately” another particular value. When such a range is expressed, other exemplary embodiments include from the one particular value and/or to the other particular value.
By “comprising” or “containing” or “including” is meant that at least the named compound, element, particle, or method step is present in the composition or article or method, but does not exclude the presence of other compounds, materials, particles, or method steps, even if the other such compounds, material, particles, or method steps have the same function as what is named.
In describing example embodiments, terminology will be resorted to for the sake of clarity. It is intended that each term contemplates its broadest meaning as understood by those skilled in the art and includes all technical equivalents that operate in a similar manner to accomplish a similar purpose. It is also to be understood that the mention of one or more steps of a method does not preclude the presence of additional method steps or intervening method steps between those steps expressly identified. Steps of a method may be performed in a different order than those described herein without departing from the scope of the present disclosure. Similarly, it is also to be understood that the mention of one or more components in a device or system does not preclude the presence of additional components or intervening components between those components expressly identified.
Some references, which may include various patents, patent applications, and publications, are cited in a reference list and discussed in the disclosure provided herein. The citation and/or discussion of such references is provided merely to clarify the description of the present disclosure and is not an admission that any such reference is “prior art” to any aspects of the present disclosure described herein. In terms of notation, “[n]” corresponds to the nth reference in the list. All references cited and discussed in this specification are incorporated herein by reference in their entireties and to the same extent as if each reference was individually incorporated by reference.
It should be appreciated that as discussed herein, a subject may be a human or any animal. It should be appreciated that an animal may be a variety of any applicable type, including, but not limited thereto, mammal, veterinarian animal, livestock animal or pet type animal, etc. As an example, the animal may be a laboratory animal specifically selected to have certain characteristics similar to human (e.g. rat, dog, pig, monkey), etc. It should be appreciated that the subject may be any applicable human patient, for example.
As discussed herein, a “subject” may be any applicable human, animal, or other organism, living or dead, or other biological or molecular structure or chemical environment, and may relate to particular components of the subject, for instance specific tissues or fluids of a subject (e.g., human tissue in a particular area of the body of a living subject), which may be in a particular location of the subject, referred to herein as an “area of interest” or a “region of interest.”
The term “about.” as used herein, means approximately, in the region of, roughly, or around. When the term “about” is used in conjunction with a numerical range, it modifies that range by extending the boundaries above and below the numerical values set forth. In general, the term “about” is used herein to modify a numerical value above and below the stated value by a variance of 10%. In one aspect, the term “about” means plus or minus 10% of the numerical value of the number with which it is being used. Therefore, about 50% means in the range of 45%-55%. Numerical ranges recited herein by endpoints include all numbers and fractions subsumed within that range (e.g. 1 to 5 includes 1, 1.5, 2, 2.75, 3, 3.90, 4, 4.24, and 5). Similarly, numerical ranges recited herein by endpoints include subranges subsumed within that range (e.g. 1 to 5 includes 1-1.5, 1.5-2, 2-2.75, 2.75-3, 3-3.90, 3.90-4, 4-4.24, 4.24-5, 2-5, 3-5, 1-4, and 2-4). It is also to be understood that all numbers and fractions thereof are presumed to be modified by the term “about.”
The invention itself, together with further objects and attendant advantages, will best be understood by reference to the following detailed description, taken in conjunction with the accompanying drawings.
These and other objects, along with advantages and features of various aspects of embodiments of the invention disclosed herein, will be made more apparent from the description, drawings and claims that follow.
The foregoing and other objects, features and advantages of the present invention, as well as the invention itself, will be more fully understood from the following description of preferred embodiments, when read together with the accompanying drawings
The accompanying drawings, which are incorporated into and form a part of the instant specification, illustrate several aspects and embodiments of the present invention and, together with the description herein, serve to explain the principles of the invention. The drawings are provided only for the purpose of illustrating select embodiments of the invention and are not to be construed as limiting the invention.
An aspect of an embodiment of the present invention provides the use of polydimethylsiloxane (PDMS) and poly(benzyl methacrylate) (PBnMA) as the two polymer species to synthesize the bottlebrush-based ABA triblock copolymer (
Table 1. Molecular parameters and mechanical properties of the 3D printable, ultrasoft, stretchable elastomers, MSC, molecular weight of side chains, nBB, number of side chains per bottlebrush, nend, number of chemical repeating units for the end linear PBnMA blocks; f, weight fraction of the end blocks; PDI, polydispersity index; G, shear modulus: γy, shear fracture strain of the elastomers, d, average distance between the centers of two neighboring domains.
An aspect of an embodiment of the present invention provides using S500 as the material for most studies. At room temperature, S500 is a solid optically transparent to the full spectra of visible light, as shown in
An aspect of an embodiment of the present invention includes the use of a stress-controlled rheometer to quantify the dynamic mechanical properties of the polymer network. Reminiscent of a perfect rubber.[31] the network exhibits nearly a frequency-independent shear storage modulus G′ (solid line circles in
Unlike conventional elastomers in which the crosslinks are permanent chemical bonds, the crosslinks in the self-assembled network are hard, glassy domains, which are physical bonds and expected to dissociate either at a high temperature or in the presence of solvents. To explore this, we monitor in real-time the viscoelasticity of the network from −20° C. to 180° C. At an oscillatory shear frequency of 1 rad/sec, the network remains a solid with G′ nearly 10 times larger than G″ (
As an alternative, we explore the effects of solvents on the dynamic mechanical properties of the elastomer. Before and after solvent reprocessing, the elastomer exhibits a negligible difference in the viscoelasticity, suggesting the material is nearly 100% reprocessable (
Using the mixture as inks, we demonstrate that the soft elastomers are amenable for direct-write printing 3D structures. The elastomers can be used to print features with a resolution of ˜0.2 mm, as visualized by the sharp edges of a printed UVA logo in
To further explore the limit of our elastomers in mechanical properties, we tune the MW of the bottlebrush block while maintaining the weight fraction of the end blocks below 6%. This ensures that the ABA polymers form a sphere microstructure.[27] By increasing the middle bottlebrush block to 1500 kDa, we create a solvent-free elastomer with a shear modulus of 60 Pa (Table 1, sample S1500 in
The extensibility of our elastomers, in the form of shear fracture strain γy, decreases with the increase of shear modulus G referenced in
Compared to all existing 3D printable elastomers (Table 2), our elastomers are of more than two orders of magnitude softer, and they can be stretched up to 6 times (
Materials. MCR-M17, monomethacryloxypropyl terminated polydimethylsiloxane, average molar mass 5000 g/mol, was purchased from Gelest and purified using basic aluminum oxide columns to remove inhibitors. Benzyl methacrylate (96%), Copper(II) chloride (CuCl2, 99.999%), Copper(II) bromide (CuBr2, 99.999%), tris[2-(dimethylamino)ethyl]amine (Me6TREN), ethylene bis(2-bromoisobutyrate (2-BiB, 97%), Tin(II) 2-ethylhexanoate (Sn(EH)2, 92.5-100%), anisole (≥99.7%) and xylene (≥99.7%) were purchased from Sigma Aldrich and used as received. Toluene (Certified ACS), methanol (Certified ACS), diethyl ether (Certified ACS), dichloromethane (DCM, Certified ACS), dimethylformamide (DMF, Certified ACS), tetrahydrofuran (THF, Certified ACS) and THF (HPLC), were purchased from Fisher and used as received.
Polymer synthesis and characterization. To synthesize a linear-bottlebrush-linear triblock copolymer, we first synthesize the middle bottlebrush block, and then use the bottlebrush as a macro-initiator to grow the end linear blocks. For both steps, we use activator regenerated by electron transfer (ARGET) atom transfer radical polymerization (ATRP),[40] as illustrated in
Here, we describe the detailed synthesis protocol using sample S500 as an example.
Step I. Synthesis of bottlebrush poly(dimethylsiloxane). A 50 mL Schlenk flask is charged with ethylene bis(2-bromoisobutyrate) (2f-BiB, 1.5 mg, 0.0042 mmol), MCR-M17 (10 g, 2 mmol), xylene (3.3 mL) and anisole (3.3 mL). We dissolve Me6TREN (46 mg, 0.2 mmol) and CuBr2 (4.5 mg, 0.02 mmol) in 1 mL dimethylformamide (DMF) to make a catalyst solution. Then, we add 30 μL catalyst solution, containing 6×10−3 mmol Me6TREN and 6×10−4 mmol CuBr2, to the mixture and bubble it with nitrogen for 60 mins to remove oxygen. Afterwards, the reducing agent, Sn (EH)2 (12.2 mg, 0.03 mmol) in 200 μL xylene, is quickly added to the reaction mixture using a glass syringe. We seal the flask and then immerse it in an oil bath at 60° C. to start the reaction. We stop the reaction after 3 hours, and a small amount of mixture is taken out to determine the conversion using proton NMR (
The rest reaction mixture is diluted with THF and passed through a neutral aluminum oxide column to remove the catalyst. The collected solution is concentrated by a rotary evaporator (Buchi R-205). To separate the bottlebrush polymer from the unreacted macromonomers, we create a co-solvent, a mixture of methanol and diethyl ether with a volume ratio 3:2, which is a good solvent for the macromonomers but not for the bottlebrush PDMS. After precipitation, we further centrifuge the mixture to separate the polymer from the solvent, re-dissolve the separated polymer in THF to make a homogenous solution. In an embodiment, the process repeats this precipitation procedure for five times to ensure that all unreacted macromonomers and impurities are completely removed. We use GPC to measure the PDI of the final product, which is 1.41 for this bbPDMS (
Step II. Synthesis of LBBL triblock copolymers. A 50 mL Schlenk flask is charged with benzyl methacrylate (BnMA, 906 mg, 5.14 mmol), macroinitiator (bbPDMS, 560 kDa, 1.34 g, 0.0024 mmol), xylene (3.9 mL) and anisole (2.6 mL). We dissolve Me6TREN (46 mg, 0.2 mmol) and CuCl2 (2.7 mg, 0.02 mmol) in 1 mL DMF to make a catalyst solution. We add 64 μL catalyst solution, containing 1.28′ 10-2 mmol Me6TREN and 1.28×10−3 mmol CuCl2, to the mixture and bubble it with nitrogen for 45 min to remove oxygen. Afterwards, reducing agent, Sn(EH)2 (25.9 mg, 6.4×10−2 mmol) in 200 μL xylene, is quickly added to the reaction mixture using a glass syringe. Then, we seal the flask and immerse it in an oil bath at 60° C. The reaction is stopped after 2 h. The reaction mixture is diluted in THF and passed through a neutral aluminum oxide column to remove the catalyst, and the collected solution is concentrated by a rotavapor. Instead of using a co-solvent as in Step I, we use methanol for precipitation for three times; this completely removes all unreacted monomers and impurities. After purification, the sample is dried in a vacuum oven (Thermo Fisher, Model 6258) at room temperature for 24 h. A small amount of the polymer is used for 1H NMR analysis and GPC analysis. From 1H NMR, the weight fraction is 6.4%, which indicates that the MW of PBnMA is about 19 kDa for each of the two end blocks. From GPC, the PDI is 1.52 for this triblock copolymer (
1H NMR characterization. 1H NMR measurements are performed using Varian-600 MHz spectrometer. Chemical shifts for 1H NMR spectra are reported in parts per million reference to a singlet at 7.26 ppm in CDCl3. We use 1H NMR to determine the number of side chains per bottlebrush and the weight fraction of PBnMA. The former one is calculated based on the conversion of PDMS macromonomers to bottlebrush PDMS, which is measured by the NMR spectra of the raw reaction mixture. The details of how to calculate the conversion of macromonomer in Step I can be found in a previous publication.[41] Examples of 1H NMR spectra of a bottlebrush PDMS and a triblock copolymer are shown in
Here we describe how to use 1H NMR to determine the number of side chains per bottlebrush and the weight fraction of PBnMA. For example, in
For this synthesis, DPbbPDMS=112, ABnMA=3.90, and APDMS=4.00; thus, DPPBnMA=218. Using this value and MWBnMA=176.21 g/mol and MWPDMS=5000 g/mol, one obtains f=0.064. And for each end of the two end blocks, MWPBzMA=19 kg/mol.
Molecular weight distribution of polymers. We use gel permeation chromatography (GPC) to determine the polydispersity index (PDI) of polymers. GPC measurements are performed using TOSOH EcoSEC HLC-8320GPC system with two TOSOH Bioscience TSKgel GMHHR-M 5 μm columns in series and a refractive index detector at 40° C. HPLC grade THF is used as the eluent with a flow rate of 1 mL/min. The calibration curve is obtained using standard polystyrene (PS) samples. The samples are dissolved in THF with a concentration around 3 mg/mL. The GPC data of all bbPDMS polymers and the corresponding LBBL polymers are shown in
To further quantify the distribution of MW, we perform modality analysis for the LBBL triblock copolymers. We find that the retention profile of sample S500 is well-described by a bimodal distribution, one minor peak with a shorter retention time at ts=11.11 min and the other major peak with a longer retention time at t1=12.06 min, as shown in
To convert the weight fraction to number fraction, one needs to determine the relation between MW ratio and the retention time ratio. For GPC, the elution volume, or time t, is linearly proportional to the logarithmic of MW.[42] Therefore, the MW of a polymer is:
where parameters a and t0 are to be determined by column calibration. Because there are no GPC standards for LBBL polymers, we use other two LBBL polymer samples S250 and S1500 with negligible shoulder peaks as the standards for calibration. The MW of middle block for these two LBBL polymers are about 250 kDa and 1500 kDa, respectively.
The average retention time is 12.61 min for S250, and that for S1500 nm is 11.36 min. Considering the MW ratio is about 6, it gives t0≈42 sec. Therefore, for the bimodal distribution of sample S500, the MW ratio between the two peaks is:
The analysis (eq. 4) suggests that the average MW of the minor component is about four times of major component in the triblock copolymer. Because the weight fraction of the minor component is about 8.7%, the corresponding number fraction is about 2.5%. As a result, the error of characteristic lengths attributed to non-monomodal distribution of polymers, if any, is only 2.5%. Thus, we conclude that the non-monomodal distribution of LBBL polymers does not affect our conclusions in both microstructure and macroscopic mechanical properties.
Grazing-incidence small-angle scattering (GISAXS). GISAXS measurements are carried out using synchrotron source at the 12-ID beamline in Brookhaven National Laboratory. To prepare thin films with controlled, uniform thicknesses, we use dynamic spin coating during which a polymer solution is dropped onto a silicon substrate rotating at a prescribed speed. For example, the sample S500 is dissolved in toluene with a concentration of 40 mg/mL. The polymer solution is purified by passing through a syringe filter with membrane pore size 0.45 μm. In parallel, a 1 cm×1 cm silicon wafer is loaded on a spin coater set with rotation per minute (RPM) of 2000 and spin time of 40 s. After reaching a stable RPM, we drop 30 μL polymer solution on the substrate. This results in a film of thickness 400 nm.
The experiments are conducted in reflection geometry using energy source of 13.9 keV. The distance between sample and detector is 8.3 m. An example of the scattered pattern and q map is shown in
Step I: synthesis of bottlebrush poly(dimethylsiloxane) (bbPDMS) using ARGET ATRP of macromonomer monomethacryloxypropyl terminated polydimethylsiloxane.
Step II: synthesis of LBBL polymer through ARGET ATRP of benzyl methacrylate (BnMA).
Practice of an aspect of an embodiment (or embodiments) of the invention will be still more fully understood from the following experimental results, which are presented herein for illustration only and should not be construed as limiting the invention in any way.
We use TEM to characterize the morphology of said elastomers. To ensure that the self-assembled microstructure is an equilibrium configuration, we use solvent-annealing to prepare the samples, during which the evaporation of the solvent is controlled at a slow rate. Specifically, a LBBL polymer sample is dissolved in toluene with a concentration of 5 mg/mL. The polymer solution is purified by passing through a syringe filter with pore size 0.45 μm. Then, 10 μL polymer solution is added to a carbon film coated copper TEM grid, which is placed on a 1 mm thick glass cover slide in a glass Petri dish partially filled with toluene. We cover the Petri dish with a glass lid to allow the solvent to slowly evaporate at room temperature for 36 h. The annealed sample is characterized using hollow-cone dark-field TEM (FEI Titan) at the electron energy of 300 keV, and a representative image of sample S500 is shown in
GISAXS measurements are carried out using synchrotron source at the 12-ID beamline in Brookhaven National Laboratory. The details of sample preparation and measurements are described in the Materials and Methods Section. The scattering results for all samples are shown in
Rheological measurements are performed using a stress-controlled rheometer (Anton Paar MCR 302) equipped with a plate-plate geometry of diameter 25 mm. We dissolve LBBL polymers in DCM at a volume ratio of 1:2 to make a homogenous mixture. We pipette about 1 mL solution onto the bottom plate, allow the solution to dry in the air at room temperature, and then heat the bottom plate to 40° C. for an additional 20 min. This allows us to prepare a dried, relatively thick film, ˜0.3 mm, yet without the formation of cavities due to the evaporation of solvent. Then, we lower the upper plate and trim the excess sample at the edge of the geometry.
For frequency sweep, we fix the temperature at 20° C. and the oscillatory shear strain at 0.5% while varying the shear frequency from 0.1 rad/sec to 10 rad/sec. For strain sweep, we fix the temperature at 20° C. and the oscillatory frequency at 1 rad/sec while increasing the shear strain from 1% to 1000%. For temperature sweep, we fix the oscillatory frequency at 1 rad/s and the shear strain at 5% while increasing the temperature from −20° C. to 180° C.
To characterize the yield stress behavior, we transfer the polymer mixture on the bottom plate and lower the upper plate to reach 0.8 mm gap distance. Then, we add deionized water to the side of the solution to prevent the solvent evaporation. The density of DCM, 1.33 g/cm3, is higher than water, and therefore this prevents convection induced mixing. During the measurement, we fix the temperature at 20° C. and the oscillatory frequency at 1 Hz while increasing the shear stress from 1 to 160 Pa.
To demonstrate the reprocessability of the self-assembled elastomers, we re-dissolve the elastomer in DCM, and re-dry the solution to obtain an elastomer. The solvent-reprocessed elastomer exhibits negligible changes in mechanical properties, as shown by
To print the soft elastomers, we modify a fused deposition modeling printer (JGAURORA Z-603S, China) by replacing the printhead with a solution extrusion module. We load the stress yield polymer mixture in a 5 mL gastight glass syringe equipped with a dispensing needle of an inner diameter 0.25 mm. The G-code and printing speed is generated and optimized using slicing software Cura 14.07.
Because our elastomers are extremely soft, the force required to deform the material is very small. To this end, we use a rheometer (Anton Paar MCR 302) with a normal force resolution of 0.5 mN to perform the compression tests. The sample, in the form of either a bulk material or a printed cubic gyroid, is fixed onto the bottom geometry. We lower the upper geometry to contact with the sample, at which the normal force is slightly above zero. During the compression measurements, the moving profile of the upper plate is pre-setup to exert cyclic and subsequent large compression at a fixed strain rate 0.005/sec. We record the normal force, gap size, and time, and calculate the stress and strain based on the pre-measured dimension of the samples.
Using the ABAQUS/Standard package, we perform FEA simulation to model the response of 3D printed features under a quasi-static compression. The elastomer is described by the Neo Hooke model, in which the strain energy density W is given by
where l1 is the first strain invariant and J is the elastic volume ratio which is defined by J=λ1λ2λ3. λi (i=1,2,3) are the principal stretches. We calibrate the simulation by comparing it to the bulk sample (
Example 1. A triblock copolymer comprising: a linear polymer wherein said linear polymer creates glassy domains within said triblock copolymer, and a bottlebrush polymer, wherein said bottlebrush polymer connects said glassy domains.
Example 2. A triblock copolymer comprising: a linear polymer, wherein said linear polymer is poly(benzyl methacrylate); and a bottlebrush polymer, wherein said bottlebrush polymer is comprised of polydimethylsiloxane side chains, wherein said bottlebrush polymer is situated between two of said linear polymers.
Example 3. A method of making a triblock copolymer, comprising: synthesizing a bottlebrush polymer; and adding one or more of said linear polymer to said bottlebrush polymer to yield said triblock copolymer.
Example 4. The method of example 3, wherein said synthesizing of said bottlebrush polymer is via free radical polymerization.
Example 5. The method of example 4, wherein synthesizing is via atom transfer radical polymerization (ATRP).
Example 6. The method of example 4 (as well as subject matter in whole or in part of example 5), wherein said atom transfer radical polymerization (ATRP) is activator regenerated electron transfer (ARGET), initiators for continuous activator regeneration (ICAR ATRP), supplemental activator and reducing agent (SARA ATRP), and electrochemically mediated ATRP.
Example 7. The method in example 3 (as well as subject matter of one or more of any combination of examples 4-6, in whole or in part), wherein starting materials of said bottlebrush polymer are ethylene bis(2-bromoisobutyrate) and monomethacryloxypropyl terminated polydimethylsiloxane.
Example 8. The method in example 3 (as well as subject matter of one or more of any combination of examples 4-7, in whole or in part), wherein said synthesizing includes a catalyst solution.
Example 9 The method of example 8, wherein said catalyst solution is comprised of. Me6TREN and CuBr2; Me6TREN and CuCl2; or Me6TREN, CuCl2 and CuBr2.
Example 10. The method of claim 8 (as well as subject matter in whole or in part of example 9), further comprising removing oxygen after said synthesis.
Example 11. The method of claim 10, further comprising adding a reducing agent.
Example 12. The method of example 11, wherein said reducing agent is: Sn(EH)2 in xylene or Sn(EH)2 in toluene.
Example 13. The method of claim 3 (as well as subject matter of one or more of any combination of examples 4-12, in whole or in part), further comprising heating during said synthesis and said addition of said one or more of said linear polymer.
Example 14. The method of example 13, where said heating is in the range of about 50 to about 70 degrees Celsius.
Example 15. The method of example 3 (as well as subject matter of one or more of any combination of examples 4-14, in whole or in part), wherein said synthesizing of said triblock copolymer is via free radical polymerization.
Example 16. The method of example 15, wherein synthesizing is via atom transfer radical polymerization (ATRP).
Example 17. The method of example 15 (as well as subject matter in whole or in part of example 16), wherein said atom transfer radical polymerization (ATRP) is activator regenerated electron transfer (ARGET), initiators for continuous activator regeneration (ICAR ATRP), supplemental activator and reducing agent (SARA ATRP), and electrochemically mediated ATRP.
Example 18. The method in example 15 (as well as subject matter of one or more of any combination of examples 16-17, in whole or in part), wherein starting materials are benzyl methacrylate, and a macroinitiator.
Example 19. The method in example 15 (as well as subject matter of one or more of any combination of examples 16-18, in whole or in part), wherein said synthesizing includes a catalyst solution.
Example 20. The method of example 15 (as well as subject matter of one or more of any combination of examples 16-19, in whole or in part), wherein said catalyst solution is comprised of: Me6TREN and CuBr2; Me6TREN and CuCl2; or Me6TREN, CuCl2 and CuBr2.
Example 21. The method of claim 15 (as well as subject matter of one or more of any combination of examples 16-20, in whole or in part), further comprising removing oxygen after said synthesizing.
Example 22. The method of claim 21, further comprising a reducing agent.
Example 23. The method of example 22, wherein said reducing agent is Sn(EH)2 in xylene or Sn(EH)2 in toluene.
Example 24. The method of claim 15 (as well as subject matter of one or more of any combination of examples 16-23, in whole or in part), further comprising heating during said synthesis and said addition of said one or more of said linear polymer.
Example 25. The method of example 24, where said heating is in the range of about 50 to about 70 degrees Celsius.
Example 26. The method of example 24, where said heating is in the range of about 60 degrees Celsius.
Example 27. A polymer network comprising a plurality of triblock copolymers, wherein: said bottlebrush polymers configured to operate as elastic network strands; and said linear polymers aggregate to form spherical glassy domains.
Example 28. The polymer network of example 27, wherein said spherical glassy domains engage in a dissociation at high temperature or in the presence of solvent, resulting in a solid-to-liquid transition of the network.
Example 29. The polymer network of example 28, wherein said dissociation is reversible.
Example 30. An article comprising the polymer network of example 27 (as well as subject matter of one or more of any combination of examples 28-29, in whole or in part).
Example 31. The article of example 30, wherein said article is a solvent-free elastomer.
Example 32. The article of example 30 (as well as subject matter in whole or in part of example 31), wherein said article is a gyroid.
Example 33. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-32, in whole or in part), wherein said article exhibits an extensibility up to 600%.
Example 34. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-33, in whole or in part), wherein said article has a Young's modulus minimum of about 100 Pa.
Example 35. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-34, in whole or in part), wherein said article is thermostable between the temperatures of about −125° C. and about 180° C.
Example 36. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-35, in whole or in part), wherein said article is 3D printable.
Example 37. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-36, in whole or in part), wherein said article contributes structurally to a medical device.
Example 38. The article of example 37, wherein said medical device is implantable.
Example 39. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-38, in whole or in part), wherein said article constitutes a portion of a vocal cord prosthesis apparatus.
Example 40. The article of example 30 (as well as subject matter of one or more of any combination of examples 31-39, in whole or in part), wherein said article constitutes a permanent filler for vesicoureteral reflux.
Example 41. A method for synthesizing a polymer network of said triblock copolymers of example 27 (as well as subject matter of one or more of any combination of examples 28-40, in whole or in part) comprising removing solvent.
Example 42. A method for 3D printing an elastomer, comprising: adding a solvent to polymer network at a specified pressure in a chamber of a 3D printer apparatus; transferring said polymer network with said solvent from a printer nozzle of said 3D printer apparatus; and wherein said solvent evaporates after exiting said nozzle and the glassy domains of said polymer network reassociate.
Example 43. A method of manufacturing any one or more of the composites or articles in any one or more of Examples 1, 2, and 27-40.
Example 44. A method of using any one or more of the composites or articles in industry in any one or more of Examples 1, 2, and 27-40.
Example 45. An article of manufacture produced by any one or more of the methods in any one or more of Examples 3-26 and 41-42.
Example 46. One or more systems configured for applying the methods in any one or more of Examples 3-26 and 41-42.
Example 47. An article of manufacture produced by any one or more of the systems in Example 46.
The devices, systems, apparatuses, modules, compositions, materials, computer program products, non-transitory computer readable medium, and methods of various embodiments of the invention disclosed herein may utilize aspects (such as devices, apparatuses, modules, systems, compositions, materials, computer program products, non-transitory computer readable medium, and methods) disclosed in the following references, applications, publications and patents and which are hereby incorporated by reference herein in their entirety (and which are not admitted to be prior art with respect to the present invention by inclusion in this section):
The devices, systems, apparatuses, modules, compositions, materials, computer program products, non-transitory computer readable medium, and methods of various embodiments of the invention disclosed herein may utilize aspects (such as devices, apparatuses, modules, systems, compositions, materials, computer program products, non-transitory computer readable medium, and methods) disclosed in the following references, applications, publications and patents and which are hereby incorporated by reference herein in their entirety (and which are not admitted to be prior art with respect to the present invention by inclusion in this section):
In summary, while the present invention has been described with respect to specific embodiments, many modifications, variations, alterations, substitutions, and equivalents will be apparent to those skilled in the art. The present invention is not to be limited in scope by the specific embodiment described herein. Indeed, various modifications of the present invention, in addition to those described herein, will be apparent to those of skill in the art from the foregoing description and accompanying drawings. Accordingly, the invention is to be considered as limited only by the spirit and scope of the following claims including all modifications and equivalents.
Still other embodiments will become readily apparent to those skilled in this art from reading the above-recited detailed description and drawings of certain exemplary embodiments. It should be understood that numerous variations, modifications, and additional embodiments are possible, and accordingly, all such variations, modifications, and embodiments are to be regarded as being within the spirit and scope of this application. For example, regardless of the content of any portion (e.g., title, field, background, summary, abstract, drawing figure, etc.) of this application, unless clearly specified to the contrary, there is no requirement for the inclusion in any claim herein or of any application claiming priority hereto of any particular described or illustrated activity or element, any particular sequence of such activities, or any particular interrelationship of such elements. Moreover, any activity can be repeated, any activity can be performed by multiple entities, and/or any element can be duplicated. Further, any activity or element can be excluded, the sequence of activities can vary, and/or the interrelationship of elements can vary. Unless clearly specified to the contrary, there is no requirement for any particular described or illustrated activity or element, any particular sequence or such activities, any particular size, speed, material, dimension or frequency, or any particularly interrelationship of such elements. Accordingly, the descriptions and drawings are to be regarded as illustrative in nature, and not as restrictive. Moreover, when any number or range is described herein, unless clearly stated otherwise, that number or range is approximate. When any range is described herein, unless clearly stated otherwise, that range includes all values therein and all sub ranges therein. Any information in any material (e.g., a United States/foreign patent, United States/foreign patent application, book, article, etc.) that has been incorporated by reference herein, is only incorporated by reference to the extent that no conflict exists between such information and the other statements and drawings set forth herein. In the event of such conflict, including a conflict that would render invalid any claim herein or seeking priority hereto, then any such conflicting information in such incorporated by reference material is specifically not incorporated by reference herein.
The present application is a national stage filing of International Application No. PCT/US2021/028987, filed Apr. 23, 2021, which claims benefit of priority under U.S.C. § 119 (e) from U.S. Provisional Application Ser. No. 63/059,779, filed Jul. 31, 2020, entitled “Ultrasoft, Stretchable, Reversible Elastomers for Direct-Write Printing Deformable Structures”; the disclosures of which are hereby incorporated by reference herein in their entirety.
This invention was made with government support under Grant No. DMR-1944625, awarded by the National Science Foundation. The government has certain rights in the invention.
Filing Document | Filing Date | Country | Kind |
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PCT/US2021/028987 | 4/23/2021 | WO |
Number | Date | Country | |
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63059779 | Jul 2020 | US |