Protein is one of the most essential and superior structural materials in nature, from cellular cytoskeleton to spider silk, highly promising in a wide range of applications including regenerative medicine, drug delivery, implantable devices, bioelectronics and biophotonics. The exceptional features of proteins, often unavailable in synthetic materials, closely relate to the manufacturing process through a controlled hierarchical self-assembly with molecule and nanoscale precision. However, it has proven to be challenging to achieve the self-assembly with the similar precision in various manufacturing techniques and three-dimensional (3D) printing, which largely rely on high energy beam/laser, high temperature, organic solvents and chemical crosslinking, thus suffering from deteriorated strength, compromised biocompatibility and limited shape complexity.
Currently, there is a need in the art for the development of manufacturing and printing techniques that maximize biocompatibility, degradability of printed structures, and minimize costs by eliminating additives and extra steps.
The present disclosure addresses the aforementioned drawbacks by providing compositions and manufacturing techniques that are based on the self-assembly of protein molecules. In general, the present disclosure provides a bio-ink composition, biocompatible 3D printed structures, a 3D printing system, and methods of using the same.
In an aspect, the present disclosure provides a three-dimensional printing method for making a three-dimensional silk article. The method includes: a) selecting an article formation parameter set including one or more silk fibroin solution parameters, one or more solvent bath parameters, one or more shear force parameters, and one or more mapping parameters; and b) iteratively introducing a silk fibroin solution into a solvent bath via a three-dimensional printing outlet, thereby forming the three-dimensional silk article. The silk fibroin solution, the solvent bath, and control of the iteratively introducing at based on the article formation parameter set. Step b) is free of photo-cross-linkers, chemical cross-linkers, and organic solvents. The method can optionally include removing the three-dimensional silk article from the solvent bath and drying the three-dimensional silk article.
One advantage of the present disclosure is to provide biocompatible 3D printed structures and 3D printing techniques that do not rely on chemical or photocrosslinking compounds, additives (e.g., organic solvents), and no external stimuli (e.g., heat). Eliminating organic solvents and chemical/photocrosslinking compounds from the manufacturing process increases the biocompatibility and degradability of printed structures, and reduces costs by eliminating additives and process steps, thereby simplifying the manufacturing process.
Another advantage of some aspects of the present disclosure is the use of induced self-assembly of protein molecules to hierarchical structures with molecule and nanoscale precision. Owing to the precise assembly, the printed structures have little defects and mechanical strength that can be maximized. Overall, this present disclosure provides a greener and more energy effective manufacturing technique for printing 3D protein structures that improves over conventional techniques that rely on high energy beam/laser, high temperature, organic solvents and chemical crosslinking (photopolymerization), thus suffering from deteriorated strength, compromised biocompatibility and limited shape complexity.
These and other advantages and features of the present invention will become more apparent from the following detailed description of the preferred embodiments of the present invention when viewed in conjunction with the accompanying drawings.
Before the present invention is described in further detail, it is to be understood that the invention is not limited to the particular embodiments described. It is also to be understood that the terminology used herein is for the purpose of describing particular embodiments only, and is not intended to be limiting. The scope of the present invention will be limited only by the claims. As used herein, the singular forms “a”, “an”, and “the” include plural embodiments unless the context clearly dictates otherwise.
Specific structures, devices and methods relating to modifying biological molecules are disclosed. It should be apparent to those skilled in the art that many additional modifications beside those already described are possible without departing from the inventive concepts. In interpreting this disclosure, all terms should be interpreted in the broadest possible manner consistent with the context. Variations of the term “comprising” should be interpreted as referring to elements, components, or steps in a non-exclusive manner, so the referenced elements, components, or steps may be combined with other elements, components, or steps that are not expressly referenced. Embodiments referenced as “comprising” certain elements are also contemplated as “consisting essentially of” and “consisting of” those elements. When two or more ranges for a particular value are recited, this disclosure contemplates all combinations of the upper and lower bounds of those ranges that are not explicitly recited. For example, recitation of a value of between 1 and 10 or between 2 and 9 also contemplates a value of between 1 and 9 or between 2 and 10.
It should be appreciated that compositions that undergo some chemical transformation during their use can be described in various ways. For instance, dissolving NaCl in water can be described as water having an NaCl concentration or water having a concentration of Na+ and Cl− ions. In the present disclosure, components of chemical compositions can be described either as the form they take prior to any chemical transformation or the form they take following the chemical transformation. If there is any ambiguity to a person having ordinary skill in the art, the assumption should be that the component is being described in the context of the particular composition being described (i.e., if describing a finished product or an intermediary after a given chemical transformation, then the chemically transformed entity is being described, and if describing a starting product or intermediary prior to the chemical transformation, then the untransformed entity is being described.
Described herein is a biomimetic process and systems for the 3D printing of proteins based on self-assembly of proteins. The advantages of this process are the direct use of proteins in water, without any crosslinkers or additives required for the process, and the aqueous ambient conditions to permit doping with bioactive components that retain function in the printed structures. Further, the printed proteinaceous structures demonstrated superior mechanical strength, optical transparency, the ability to form complicated 3D geometries and cytocompatibility; all demonstrated with the fabrication of functional microfluidic chips. In one aspect, the 3D printing method described herein employs shear stress and solvent effects to induce the self-assembly of protein molecules at multiple scales, which allows a 3D printing-compatible phase-transition from soluble ink to insoluble filament. The 3D printed structures may be optimized to feature a desirable combination of macroscopic physical properties (mechanical strength, elasticity and optical transparency) and biocompatibility (endothelization, controlled degradation and preservation of labile enzymes).
Referring to
Before the three-dimensional silk article has been dried or in the absence of drying, the wet article can have impressive elastic modulus or Young's modulus, ultimate stress (i.e., ultimate tensile strength), tensile toughness, ultimate strain (i.e., tensile strain), beta-sheet content, beta-turn content, transmittance, and/or combinations thereof.
In some cases, the wet article can have an elastic modulus or Young's modulus of at least 10 MPa, at least 20 MPa, at least 30 MPa, at least 40 MPa, at least 50 MPa, at least 60 MPa, at least 70 MPa, at least 80 MPa, at least 90 MPa, at least 100 MPa, at least 105 MPa, at least 110 MPa, at least 115 MPa, at least 120 MPa, at least 125 MPa, at least 130 MPa, at least 140 MPa, at least 150 MPa, at least 160 MPa, at least 170 MPa, at least 180 MPa, at least 190 MPa, at least 200 MPa, or greater. In some cases, the wet article can have an elastic modulus or Young's modulus of at most 1000 MPa, at most 950 MPa, at most 900 MPa, at most 850 MPa, at most 800 MPa, at most 750 MPa, at most 700 MPa, at most 650 MPa, at most 600 MPa, at most 550 MPa, at most 500 MPa, at most 450 MPa, at most 400 MPa, at most 350 MPa, at most 325 MPa, at most 300 MPa, at most 275 MPa, at most 250 MPa, at most 225 MPa, at most 200 MPa, at most 175 MPa, at most 150 MPa, at most 125 MPa, at most 100 MPa, or lower.
In some cases, the wet article can have an ultimate stress (i.e., an ultimate tensile strength) of at least 0.1 MPa, at least 0.5 MPa, at least 1 MPa, at least 5 MPa, at least 10 MPa, at least 25 MPa, at least 30 MPa, at least 35 MPa, at least 40 MPa, at least 45 MPa, at least 50 MPa, at least 55 MPa, at least 60 MPa, at least 65 MPa, at least 70 MPa, at least 75 MPa, or greater. In some cases, the dried article can have an ultimate stress of at most 100 MPa, at most 95 MPa, at most 90 MPa, at most 85 MPa, at most 80 MPa, at most 75 MPa, at most 70 MPa, at most 65 MPa, at most 60 MPa, at most 55 MPa, at most 50 MPa, at most 45 MPa, at most 40 MPa, at most 35 MPa, at most 30 MPa, at most 25 MPa, or lower.
In some cases, the wet article can have an ultimate strain (i.e., an ultimate tensile strain) or extensibility of at least 35.0%, at least 40.0%, at least 45.0%, at least 50.0%, at least 55.0%, at least 60.0%, at least 65.0%, at least 70.0%, at least 75.0%, at least 80.0%, at least 85.0%, at least 90.0%, at least 95.0%, at least 100.0%, at least 105.0%, at least 110.0%, at least 115.0%, at least 120.0%, at least 125.0%, at least 130.0%, at least 140.0%, at least 150.0%, at least 160.0%, at least 170.0%, at least 180.0%, at least 190.0%, at least 200.0%, at least 250.0%, or greater. In some cases, the dried article can have an ultimate strain of at most 500.0%, at most 450.0%, at most 400.0%, at most 350.0%, at most 300.0%, at most 250.0%, at most 200.0%, at most 150.0%, at most 140.0%, at most 130.0%, at most 120.0%, at most 110.0%, at most 100.0%, at most 95.0%, at most 90.0%, at most 85.0%, at most 80.0%, at most 75.0%, or lower.
In some cases, the wet article can include silk fibroin having a β-sheet content of less than 10%, less than 9%, less than 8%, less than 7.5%, less than 7%, less than 6.5%, less than 6%, less than 5.5%, less than 5%, less than 4.5%, less than 4%, less than 3.5%, less than 3%, less than 2.5%, less than 2%, less than 1.5%, less than 1%, less than 0.5%, or lower. In some cases, the dried article can include silk fibroin having a β-turn content of greater than 5%, greater than 10%, greater than 15%, greater than 20%, greater than 25%, greater than 30%, or higher.
In some cases, the wet article can have a visible light transmittance of at least 80.0%, at least 82.5%, at least 85.0%, at least 87.5%, at least 90.0%, at least 91.0%, at least 92.0%, at least 93.0%, at least 94.0%, at least 95.0%, at least 96.0%, at least 97.0%, at least 98.0%, at least 99.0%, or greater. In other cases, the dried article can have a lower visible light transmittance, including cases where a dye or opacifying agent has been added to the ink prior to printing.
After the three-dimensional silk article has been dried, the dried article can have impressive elastic modulus or Young's modulus, ultimate stress (i.e., ultimate tensile strength), tensile toughness, ultimate strain (i.e., tensile strain), beta-sheet content, beta-turn content, transmittance, and/or combinations thereof.
In some cases, the dried article can have an elastic modulus or Young's modulus of at least 0.1 GPa, at least 0.2 GPa, at least 0.3 GPa, at least 0.4 GPa, at least 0.5 GPa, at least 0.6 GPa, at least 0.7 GPa, at least 0.8 GPa, at least 0.9 GPa, at least 1.0 GPa, at least 1.1 GPa, at least 1.2 GPa, at least 1.3 GPa, at least 1.4 GPa, at least 1.5 GPa, at least 1.6 GPa, at least 1.7 GPa, at least 1.8 GPa, at least 1.9 GPa, at least 2.0 GPa, at least 2.25 GPa, at least 2.5 GPa, at least 2.75 GPa, at least 3.0 GPa, at least 3.5 GPa, at least 4.0 GPa, at least 4.5 GPa, at least 5.0 GPa, or greater. In some cases, the dried article can have an elastic modulus of at most 10.0 GPa, at most 9.5 GPa, at most 9.0 GPa, at most 8.5 GPa, at most 8.0 GPa, at most 7.5 GPa, at most 7.0 GPa, at most 6.75 GPa, at most 6.5 GPa, at most 6.25 GPa, at most 6.0 GPa, at most 5.75 GPa, at most 5.5 GPa, at most 5.25 GPa, at most 5.0 GPa, at most 4.75 GPa, at most 4.5 GPa, at most 4.25 GPa, at most 4.0 GPa, at most 3.75 GPa, at most 3.5 GPa, at most 3.25 GPa, at most 3.0 GPa, at most 2.75 GPa, at most 2.5 GPa, at most 2.25 GPa, at most 2.0 GPa, at most 1.75 GPa, at most 1.5 GPa, at most 1.25 GPa, at most 1.0 GPa, or lower.
In some cases, the dried article can have an ultimate stress (i.e., an ultimate tensile strength) of at least 1 MPa, at least 5 MPa, at least 10 MPa, at least 25 MPa, at least 30 MPa, at least 35 MPa, at least 40 MPa, at least 45 MPa, at least 50 MPa, at least 55 MPa, at least 60 MPa, at least 65 MPa, at least 70 MPa, at least 75 MPa, at least 100 MPa, or greater. In some cases, the dried article can have an ultimate stress of at most 500 MPa, at most 450 MPa, at most 400 MPa, at most 350 MPa, at most 300 MPa, at most 250 MPa, at most 200 MPa, at most 150 MPa, at most 125 MPa, at most 100 MPa, at most 95 MPa, at most 90 MPa, at most 85 MPa, at most 80 MPa, at most 75 MPa, at most 70 MPa, at most 65 MPa, at most 60 MPa, or lower.
In some cases, the dried article can have an ultimate strain (i.e., an ultimate tensile strain) or extensibility of at least 0.1%, at least 0.2%, at least 0.3%, at least 0.4%, at least 0.5%, at least 0.6%, at least 0.7%, at least 0.8%, at least 0.9%, at least 1.0%, at least 1.25%, at least 1.50%, at least 1.75%, at least 2.0%, at least 2.5%, at least 3.0%, at least 3.5%, at least 4.0%, at least 4.5%, at least 5.0%, at least 6.0%, at least 7.0%, at least 8.0%, at least 9.0%, at least 10.0%, or greater. In some cases, the dried article can have an ultimate strain of at most 50.0%, at most 45.0%, at most 40.0%, at most 35.0%, at most 30.0%, at most 25.0%, at most 20.0%, at most 15.0%, at most 14.0%, at most 13.0%, at most 12.0%, at most 11.0%, at most 10.0%, at most 9.5%, at most 9.0%, at most 8.5%, at most 8.0%, at most 7.5%, at most 7.0%, at most 6.5%, at most 6.0%, at most 5.5%, at most 5.0%, at most 4.5%, at most 4.0%, at most 3.5%, at most 3.0%, at most 2.5%, or lower.
In some cases, the dried article can include silk fibroin having a β-sheet content of greater than 5%, greater than 10%, greater than 15%, greater than 20%, greater than 25%, greater than 30%, greater than 35%, greater than 37.5%, greater than 40%, greater than 41%, greater than 42%, greater than 43%, greater than 44%, greater than 45%, greater than 46%, greater than 47%, greater than 48%, greater than 49%, greater than 50%, greater than 51%, greater than 52%, greater than 53%, greater than 54%, greater than 55%, greater than 60%, greater than 65%, greater than 70%, greater than 75%, greater than 80%, greater than 85%, greater than 90%, or higher. In some cases, the dried article can include silk fibroin having a β-turn content of less than 15%, less than 14%, less than 13%, less than 12%, less than 11%, less than 10%, less than 9%, less than 8%, less than 7.5%, less than 7%, less than 6.5%, less than 6%, less than 5.5%, less than 5%, less than 4.5%, less than 4%, less than 3.5%, less than 3%, less than 2.5%, less than 2%, less than 1.5%, less than 1%, less than 0.5%, or lower.
In some cases, the dried article can have a visible light transmittance of at least 80.0%, at least 82.5%, at least 85.0%, at least 87.5%, at least 90.0%, at least 91.0%, at least 92.0%, at least 93.0%, at least 94.0%, at least 95.0%, at least 96.0%, at least 97.0%, at least 98.0%, at least 99.0%, or greater. In other cases, the dried article can have a lower visible light transmittance, including cases where a dye or opacifying agent has been added to the ink prior to printing.
The 3D printing method of the present disclosure can include selecting an article formation parameter set including one or more insoluble ink parameters, one or more solvent bath parameters, one or more shear force parameters, and one or more mapping parameters. In one aspect, the insoluble ink can be a silk fibroin solution. The silk fibroin solution parameter can include the group consisting of silk fibroin concentration, silk fibroin molecular weight distribution, and combinations thereof. The silk fibroin solution can have a silk fibroin concentration between 10 wt % and 40 wt %, or between 15 wt % and 40 wt %, or between 20 wt % and 40 wt %, or between 25 wt % and 40 wt %, or between 30 wt % and 40 wt %. The silk fibroin solution can have a silk fibroin concentration between 10 wt % and 40 wt %, or between 10 wt % and 35 wt %, or between 10 wt % and 30 wt %, or between 10 wt % and 25 wt %, or between 10 wt % and 20 wt %. The molecular weight distribution of the silk fibroin can be at least 10 kDa, 20 kDa, 30 kDa, 40 kDa, 50 kDa, 60 kDa, 70 kDa, 80 kDa, 90 kDa, or another minimum value understood by those having ordinary skill in the art to be a useful value for preparing a silk fibroin solution for 3D printing. The molecular weight cut-off can be at most 450 kDa, 400 kDa, 350 kDa, 300 kDa, 250 kDa, 200 kDa, 150 kDa, 100 kDa, 90 kDa, or another maximum value understood by those having ordinary skill in the art to be a useful value for preparing a silk fibroin solution for 3D printing.
In one aspect, the solvent bath parameters can include a parameter selected from the group consisting of a chemical composition of the solvent bath, a soak time, pH, temperature and combinations thereof.
In one aspect, the chemical composition of the solvent bath comprises one or more salts. In one non-limiting example, the solvent bath can contain a total salt concentration of at least 500 mM, or at least 1 M, or at least 2 M, or at least 3 M, or at least 4 M, or at least 5 M. In another non-limiting example, the solvent bath can contain a total salt concentration of at most 10 M, at most 8 M, at most 7 M, at most 6 M, or at most 5 M, or at most 4 M, or at most 3M, or at most 2 M, or at most 1 M. In another non-limiting example, the one or more salts are selected from the group consisting of sodium chloride, dipotassium phosphate, ammonium sulfate, and combinations thereof. In some cases, the solvent bath include sodium chloride at a concentration of 5.0 M or lower. In some cases, the solvent bath includes dipotassium phosphate at a concentration of 2.0 M or lower. In some cases, the solvent bath includes ammonium sulfate at a concentration of 2.25 M or lower. In one specific example, the solvent bath is a solution containing 0.5 M dipotassium phosphate and 4 M sodium chloride. In some cases, the solvent bath includes potassium ions and sodium ions. In some cases, the solvent bath includes potassium ions in a concentration of between 0.1 M and 2.0 M. In some cases, the solvent bath includes sodium ions in a concentration of between 3.0 M and 5.0 M. In comes cases, the solvent bath has an osmolarity of at least 8 M, at least 9 M, at least 10 M, or at least 12 M. In some cases, the solvent bath has an osmolarity of at most 20 M, at most 16 M, or at most 12 M.
In another aspect, the pH of the solvent can be at least 2.5, 3, 3.5, 4, 4.5, 5, 5.5, 6, 6.5, 7, or anther minimum value understood by those having ordinary skill in the art to be a useful value of preparing a solvent bath for 3D printing of silk fibroin. In another aspect, the pH of the solvent can be at most 7.5, 7, 6.5, 6, 5.5, 5, or anther maximum value understood by those having ordinary skill in the art to be a useful value for preparing a solvent bath for 3D printing of silk fibroin. In some cases, the solvent bath has a pH of between 4 and 7 or between 5 and 7.
In one aspect, the solvent bath is at a temperature of 20° C., or 25° C., or 30° C., or 35° C., or 40° C., or a temperature between these values. In some cases, the solvent bath is at room temperature.
In one embodiment, the silk fibroin solution or protein ink is an aqueous solution. In some cases, the silk fibroin solution or protein ink includes silk fibroin or other protein in an amount by weight of at least 10%, at least 15%, at least 20%, at least 25%, at least 30%. In some cases, the silk fibroin solution or protein ink includes silk fibroin or other protein in an amount by weight of at most 40%, at most 37.5%, at most 35%, at most 32.5%, at most 30%, or at most 25%.
The 3D printing method of the present disclosure can further include iteratively introducing a silk fibroin solution into a solvent bath via a three-dimensional printing outlet, thereby forming the three-dimensional silk article, wherein the silk fibroin solution, the solvent bath, and control of the iteratively introducing are based on the article formation parameter set.
The mapping parameters of the 3D printing method of the present disclosure can include locations and volumes at which the silk solution is introduced though the fine nozzle into the saline bath. In one aspect, the mapping parameter can include a nozzle movement speed. In another aspect, the one or more mapping parameter are selected by converting a three-dimensional digital image file into the one or more mapping parameters through a computer, wherein the computer is in electronic communication with a printer.
Suitable printers may include a commercial extrusion-based 3D printer from Cellink, Sweden. In one aspect, the extrusion rate of the 3D printer is controlled by compressed air and valves to enter shear thinning region, which is obtained in a viscosity-shear rate profile. In one aspect, the shear rate during extrusion is higher than that of natural, in vivo silk spinning which is between 1-10 seconds−1, or between 2-10 seconds−1, or between 4-10 seconds−1, or between 6-10 seconds−1, or between 8-10 seconds−1. In some aspects, the protein ink is loaded into a syringe (3 ml) equipped with a fine nozzle with an inner diameter of between 5 μm to 500 μm, or between 50 μm to 100 μm, or between 100 μm to 250 μm, or between 200 μm to 300 μm, or between 300 μm to 400 μm, or between 400 μm to 450 μm, or any other combination of lower and upper bounds between this list. The printing head may be controlled to move at a speed from 0.1 to 10 mm/s, or from 0.2 to 10 mm/s, or from 0.5 to 10 mm/s, or from 1 to 10 mm/s, or from 3 to 10 mm/s, or from 5 to 10 mm/s. The prints may be harvested from the saline solution after 1-5 days, or 2-5 days, or 3-5 days, or 4-5 days for freeze drying or critical point drying, followed by a variety of characterizations of morphology, mechanics, optics and biocompatibility.
The silk fibroin solution of the 3D printing method of the present disclosure can further include an additive. In one aspect, the additive can be selected from the group consisting of a mammalian cell, a bioactive molecule, an antibody, an antibiotic, a nanoparticle, dyes, and combinations thereof. In one non-limiting example, the mammalian cell may comprise a human umbilic vein endothelial cell (HUVEC). In another non-limiting example, the bioactive molecule may comprise horseradish peroxidase. In another non-limiting example, the antibiotic may comprise ampicillin. In another non-limiting example, the nanoparticle can be selected from the group consisting of a gold, quantum dots, and combinations thereof. In another non-limiting example, the dye may comprise a fluorescent dye.
In some aspects, the addition of saline solution increases the storage modulus (G′) of the protein ink by more than a thousand-fold, as shown in
a Materials Letters 60 (2006) 919
The transmittance of 3D print is above 80% over visual range (
The 3D protein prints demonstrated robust mechanical properties and structural integrity. A two-layer structure in a dog-bone shape was designed and printed for uniaxial tensile tests (
3D Protein-based prints can provide a structural basis for support, as well as for a variety of biofunctions (
Degradability and biocompatibility may be useful features for protein structures, such as implants. The degradation profiles of different protein lattices are shown in
The silk article of the 3D printing method of the present disclosure can be selected from the group consisting of a degradable structure, a device, a system, a microfluidic chip, a hollow Y-shape tube, a blood vessel, a nerve conduit, an implantable scaffold, an optical lens, and combinations thereof.
The following examples set forth, in detail, ways in which the flexible composite material may be synthesized, and will enable one of skill in the art to more readily understand the principles thereof. The following examples are presented by way of illustration and are not meant to be limiting in any way.
Preparation of Protein Ink and 3D Printing Procedure
The protein ink was prepared using 5 g of sliced cocoons from Bombyx mori (Tajima Shoji Co., Yokohama, Japan) were degummed in 2 L boiling solution of 0.02 M sodium carbonate for 30 min. The degummed fibers were dried overnight and solubilized in 9.3 M lithium bromide for 4 h in a 60° C. oven, followed by a dialysis (MWCO, 3,500) against DI water with 6 changes over 3 days. The insoluble particulates were removed by centrifugation (two times at 9,000 rpm, 20 min, 4° C.) and syringe filtration (low protein binding PVDF membrane, 5 μm, Merck Millipore, Ireland). The filtered solution was loaded into Slide-a-Lyzer dialysis cassettes (MWCO 3,500, Pierce) and concentrated by drying under 4° C. for 8 days to obtain high concentrations from 14 wt % to 30 wt %. Silk concentration was determined by weighing a dried sample of a known volume. The ink was doped with HRP, ampicillin or nanomaterials (Quantum dots and gold nanorods (10 nm, 808 mm, Sigma)) at certain ratios. When printing, the ink was loaded into a 3 ml syringe (EFD, Inc., RI, USA) quipped with a 33-gauge dispensing tip (EFD, Inc., RI, USA). 3D printing was performed with an Inkredible printer (Cellink, Sweden), coupled with an open-source software, Repetier host, and compressed air pump. All printing geometries were controlled by manually written G-code commands.
Morphology Characterization
Atomic force microscopy (AFM) was performed by using the Asylum Research Cypher AFM in an AC mode in air at scan rates of 2.44 or 0.8 Hz and aluminum coated silicon cantilevers (300 kHz and 40 N/m, nominal values) (Budget Sensors, USA). AFM images were processed by Gwyddion. Scanning Electronic microscopy (SEM) imaging was performed using an Ultra 55 field-emission SEM, Carl Zeiss AG, at an acceleration voltage of 5-8 kV. All SEM specimens were coated with a 5-10 nm thick Pt/Pd (80:20).
Rheology Characterization and Model Fitting
Rheology was performed on an ARES-LS2 (TA Instruments, New Castle, Del.) using a pair of 25 mm stainless steel parallel plates. To prevent evaporation during testing, mineral oil was placed around the plates. Dynamic strain sweep was performed to obtain the linear viscoelastic region (LVR). Dynamic time sweep chooses 1% strain from the LVR and is preformed to demonstrate 1) the stability of the ink; and 2) the solvent effect by pipetting the saline around the plates. The viscosity-shear rate curves were fitted using simplified Carreau-Yasuda model (Equation 1) and Hershel-Buckley model (Equation 2) at low and high shear rate regions, respectively:
where viscosity (η) is a function of shear rate ({dot over (γ)}), η0 is the zero-shear viscosity, TO is the yield stress, K is the consistency factor, α and n are indexes.
FTIR Characterization
The structures of the printing ink and prints were characterized by FTIR spectroscopy in ATR mode (Jasco FTIR-6200, Jasco Instruments, Easton, Md.). For each measurement, 64 times of scanning was utilized with a nominal resolution of 4 cm−1. Spectral corrections and deconvolution were performed using a home-developed MATLAB package. The spectra were first smoothed with a 5-point triangle smoothing method and then baseline corrected using a cubic spline for the amide I band. The deconvolution was performed with a secondary derivative method. The secondary structure analysis was performed according to the literature (Guo et al. Biomacromolecules 2018, 19, 906-917)
Mechanical Testing
The mechanical tests of the dog-bone shaped protein prints were carried out by using an Instron 3366 machine (Instron, Norwood, USA) in tensile mode in a water cup with a tensile speed of 0.13 mm/s. The prints were griped at the expanded regions at both ends. The cross-section area was calculated in ImageJ based on SEM images of the prints that were manually snapped in liquid nitrogen.
In Vitro Enzymatic Degradation
The in vitro degradation of the 3D proteinaceous prints (in the shape of a ¾ sphere with 3 mm diameter) was evaluated using protease XIV (P8811, Sigma-Aldrich) with an activity of 6.7 U/mg. 3D prints were immersed in 5 ml of phosphate buffer saline (pH 7.4) containing protease (1U or 20 U) at 37° C. The enzyme solution was replaced with newly prepared solution every 24 h. After the specific time, samples were washed with phosphate buffer saline and distilled water, followed by lyophilization, weighing and SEM imaging. For controls, samples were immersed in phosphate buffer saline without enzyme.
Cell Culture and Imaging
Primary Human umbilical vein endothelial cells (HUVECs, C2519A, Lonza) were cultured in EGM™-2 BulletKit™ Medium (Lonza) to reach ˜80% confluence till passage 4. Then, HUVECs were harvested and seeded on the protein prints at 3×106 cell/100 μl. After 5 days, the cells and prints were fixed and dyed with DAPI and Alexa Fluor™ 488 Phalloidin (Thermo Scientific, USA), followed by imaging with a Leica SP8 confocal microscope (Leica microsystems, Germany). Images were processed using ImageJ (NIH).
Preparation of Protein Ink and 3D Printing Procedure
The protein ink was prepared using 5 g of sliced cocoons from Bombyx mori (Tajima Shoji Co., Yokohama, Japan) were degummed in 2 L boiling solution of 0.02 M sodium carbonate for 30 min. The degummed fibers were dried overnight and solubilized in 9.3 M lithium bromide for 4 h in a 60° C. oven, followed by a dialysis (MWCO, 3,500) against DI water with 6 changes over 3 days. The insoluble particulates were removed by centrifugation (two times at 9,000 rpm, 20 min, 4° C.) and syringe filtration (low protein binding PVDF membrane, 5 μm, Merck Millipore, Ireland). The filtered solution was loaded into Slide-a-Lyzer dialysis cassettes (MWCO 3,500, Pierce) and concentrated by drying under 4° C. for around 8 days to obtain high concentrations around 30 wt %. Silk concentration was determined by weighing a dried sample of a known volume. The ink was doped with horseradish peroxidase (HRP)-, labeled antibody (A0293, Sigma-Aldrich) in 1:1000, rhodamine B (79754, Sigma-Aldrich, saturated solution) in 1:100, Fluorescein (46955, Sigma-Aldrich, saturated solution) in 1:100 and Quantum dots (900225, Sigma-Aldrich) in 1:100 by stirring for 2 minutes and settling for 1-2 hours till all bubbles disappear. The solution of silk fibroin, as printing ink, was a viscous yellowish clear liquid with ˜6% β-sheet content, ˜30 wt % concentration, pH ˜7 and ˜90 kDa molecular weight, analogous to native silk protein dope except for the lower molecular weight (˜90 kDa vs. ˜300 kDa). The hydrodynamic diameter of the diluted ink was around 23 nm, suggesting a single molecular dispersion. Rheological characterization of the ink showed typical shear-thinning behavior (FIG. 11a). We further used the Herschel-Bulkley (HB) model to fit viscous-shear rate profiles at the region of high shear rate (>0.1 s−1), as well as finite element analysis (FEA) to simulate the rheological behavior of the ink in the nozzle during 3D printing. At a printing pressure of 210 kPa, the viscosity decreased by nearly a hundred-fold (from 547.22 Pa·s to 6.18 Pa·s) and the simulated shear rate reached ˜65 s−1, above in vivo critical values (˜1-10 s−1), indicating the elongation of protein molecules during 3D printing, mimicking native silk spinning.
De Novo Aqueous Salt Bath
As the crux of this work, we rationally developed an aqueous bath with a de novo composition of inorganic salts (0.5 M dipotassium phosphate and 4 M sodium chloride) to recapitulate solvent conditions of silk spinning by two evolutionarily-distant species, spiders and silkworms. The chemical composition as well as the working mechanism to solidify ink of this bath is essentially different from others for wet spinning and 3D printing for proteins and polymers as shown in Table 4. First, the bath is composed of the most abundant salt ions in the spinning glands, such as potassium and sodium. We assume that the metal ions participate the spinning of silks perhaps by imposing specific effects on proteins through interacting with water molecules on protein surfaces other than forming ionic bonds. Second, the bath is of a slightly acidic pH (˜6) and high osmolarity (>8 M, as one sodium chloride molecule disassociates into two ions) to remove water from extruded ink, which recapitulates solvent conditions of acidification and dehydration for silk spinning. Notably, the concentration of ions at the site of silk fiber formation remains unknown, and dehydration via elevated osmolarity is indeed a general principle found in animals, for example in urine concentration. Third, the bath was optimized to tune the dynamics of molecular crosslinking\assembly, tightly related to the phase-transition of the ink from liquid to gel and characterized by changes of storage modulus (G′) (
Ordered and Hierarchical Structure
Ordered hierarchical organization of molecules is a characteristic of directed molecular assembly (
Mechanic and Optic Performance
A 3D printed 4-layer lattice (in wet) is of compliance, extensibility and durable junctions between layers that remain intact under repeatedly stretching and folding. To characterize the mechanical performance in uniaxial tensile tests, single filaments of ˜30 mm in length were directly cut from a seven-layer 3D print without post-stretching (
The dense morphology allows 3D prints visually transparent, such as the vase and lattice and membrane (
a Estimated from published stress-strain curves;
Biocompatible and Multi-Material Printing
The whole process of 3D printing is at ambient and aqueous conditions, which is highly desired to preserve the biodegradability and cytocompatibility as well as the integrated biofunctions of 3D proteinaceous prints, because harsh processing conditions and toxic organic solvent probably deteriorate these properties. The biodegradability was investigated in the proteolytic degradation of the prints (
Microfluidic Channels
We further demonstrated the manufacturing capability by constructing a bifurcate and perfusable microfluidic channel in a single-step manner (
Morphology and Polarized Optical Microscopy Characterization
3D prints were dried in a critical point dryer (CPD 300, Leica, Germany) and coated with a 5-10 nm thick Pt/Pd (80:20), followed by scanning electronic microscopy (SEM) imaging (Ultra 55 field-emission SEM, Carl Zeiss AG, Germany) at an acceleration voltage of 5 kV. The cross-section of 3D printed filaments was obtained from breaking in liquid nitrogen or tensile test. The cross-section of 3D printed microfluidic channels was imaged with a Leica SP8 confocal microscope using the autofluorescence of the assembled silk fibroin. The polarized optical microscopy (Eclipse E200POL, Nikon, Japan) equipped with a first order red retardation plate was used to image birefringence of 3D prints.
Rheology Characterization and Model Fitting
Rheology was performed on an ARES-LS2 (TA Instruments, New Castle, Del.) using a 25 mm stainless steel cone with an angle of 0.0994° and a gap of 0.0468 mm and a 50 mm stainless steel plain plate. Static strain sweeps were performed to obtain the viscosity-shear rate curve. Part of the curve (at shear rate >0.1 s−1) was fitted with Herschel-Bulkley (HB) model, as shown below:
where viscosity (η, Pa·s) is a function of shear rate ({dot over (γ)}, s−1), τ0 is the yield stress (Pa), K is a consistency factor (Pa·s1-n), and n is an index. The fitted values of τ0, K and n are 0.683 Pa, 9.707 Pa·s1−n and 0.852, respectively.
Finite Element Analysis (FEA) was performed with COMSOL Multiphysics 5.3a (COMSOL Inc., MA) using the fitted parameters and experimentally measured flow rates at printing pressures ranging from 50 kPa to 300 kPa. A 2D symmetry model of the nozzle was established and meshed into 16,000 triangle elements. The results were reconstructed in 2D and 3D by mirroring and revolving, respectively. The quantitative data of viscosity and shear rate were calculated from averaging the value of each element in the whole simulated model.
We performed oscillatory time sweep at 1 Hz and 1% strain (within the linear viscoelastic region) for 5 min. At ˜140s, 100 μl of the printing bath, 5M dipotassium phosphate or DI water was pipetted around the circumstance of the cone for evaluating the dynamics of the molecular assembly.
Fourier Transform Infrared Spectroscopy (FTIR) Characterization
The secondary structures of proteins (β-sheet, random coil/helix and β-turn) of the printing ink and the prints (both lyophilized) were characterized by FTIR spectroscopy in ATR mode (FTIR-6200, Jasco Instruments, Easton, Md.) and analyzed by semi-qualitative spectral deconvolution of amide I band (1,580-1,720 cm−1) according to previous reports. For each measurement, 64 scans were co-added with a nominal resolution of 4 cm−1.
Raman Microscopy
The cross-sectional line profile of the printed filament was characterized with a confocal microscope equipped with a Horiba Multiline Raman Spectrometer (Horiba scientific, Japan). The Raman spectrometer contains 633 nm He—Ne diode laser (˜2 mW), 600 gr/mm grating and Synapse CCD detector. Raman spectrums were obtained at 20 points, separated by 5 μm, with exposure time of 30 seconds and twice accumulations at each point. Data acquisition was automatically denoised and controlled by Lab Spec 6 software (Horiba scientific, Japan). The peak area between 1664 cm−1 to 1668 cm−1 was used to estimate the content of β-sheet.
Morphology and Polarized Optical Microscopy
3D prints were dried in a critical point dryer (CPD 300, Leica, Germany) and coated with a 5-10 nm thick Pt/Pd (80:20), followed by scanning electronic microscopy (SEM) imaging (Ultra 55 field-emission SEM, Carl Zeiss AG, Germany) at an acceleration voltage of 5 kV. The cross-section of 3D printed filaments was obtained from breaking in liquid nitrogen or tensile test. The cross-section of 3D printed microfluidic channels was imaged with a Leica SP8 confocal microscope using the autofluorescence of the assembled silk fibroin. The polarized optical microscopy (Eclipse E200POL, Nikon, Japan) equipped with a first order red retardation plate was used to image birefringence of 3D prints.
Transparency
For light transmission measurements, visible spectra were taken using a vis/near-infrared fiber-optic spectrometer (USB-2000, Ocean Optics, USA). White light was propagated through the fiber to pass through a 3D printed membrane composed of parallel and conterminous filaments, and the transmitted light was coupled into a fiber tip guided to the spectrometer. The distance between the illumination source and the collection tip was fixed at 10 mm.
Mechanical Testing
Single filaments of ˜30 mm length obtained from air-dried seven-layer 3D prints were used for uniaxial tensile test with Instron 3366 (Instron, USA) at cross-head speeds of 0.13 mm/s (for wet samples) and 0.013 mm/s (dry). The use of the single filament isolates the influence of local orientation and filled density. All filaments were dry. For wet samples, we hydrated dried filaments in DI water for 5 minutes. The ends of the filament were clamped in a pair of pneumatic grips (2752-005, Instron). Tensile strength and toughness were calculated based on the cross-sectional area of the filaments was measured from SEM images after snapping in liquid nitrogen. Elastic modulus was calculated from the initial range of strain (5%-10% for dry samples and 0%-5% for wet ones).
The present disclosure has described one or more preferred embodiments, and it should be appreciated that many equivalents, alternatives, variations, and modifications, aside from those expressly stated, are possible and within the scope of the invention.
This application is related to, claims priority to, and incorporated herein by reference for all purposes U.S. Provisional Patent Application No. 62/720,016, filed Aug. 20, 2018.
This invention was made with government support under grant EB002520 awarded by the National Institutes of Health. The government has certain rights in the invention.
Filing Document | Filing Date | Country | Kind |
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PCT/US2019/047359 | 8/20/2019 | WO | 00 |
Number | Date | Country | |
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62720016 | Aug 2018 | US |