Embodiments relate to granular hydrogel bioinks with preserved interconnected porosity for applications, such as extrusion bioprinting, and methods of use and making thereof.
Hydrogels have enabled the development of bioinks for tissue engineering and regeneration via providing physiochemically versatile tissue-mimetic microenvironments. Fabricated from polymer chains and/or colloidal particles, bulk hydrogels commonly attain nanoscale pores, limiting oxygen and metabolite diffusion and cell infiltration in thick three-dimensional (3D) constructs. As an example, a hydrogel scaffold fabricated from a purely elastic network of crosslinked polymers with a storage modulus G′ in the order of 10 kPa, mimicking soft tissues, will have pores in the order of ξ˜(G′/kBT)−1/3˜10 nm at physiological temperature. Here, kB is the Boltzmann constant, and T denotes absolute temperature. Extensive efforts have been devoted to imparting microscale pores to hydrogels, most of which rely on non-bioorthogonal approaches, such as using porogens (e.g., salt crystals), ice-templating, or foaming. The main limitation of 3D bioprinting using conventional bulk hydrogel bioinks is the trade-off between shape fidelity and cell viability that is regulated by hydrogel stiffness/porosity.
According to the traditional “biofabrication window,” increasing the hydrogel stiffness, e.g., via increasing polymer concentration and/or crosslinking density, improves the construct shape fidelity while compromising the cell viability via reduced porosity.
To overcome the structural limitations of bulk hydrogels, microgels have been engineered as building blocks to assemble tissue engineering scaffolds, leveraging cell-scale interconnected microporosity and seamless cell infiltration. Granular hydrogel scaffolds have introduced a new biomaterial paradigm for tissue engineering, accelerating the regeneration of tissues, including skin, brain, and heart. These newly emerged scaffolds provide several unique advantages over bulk hydrogels, including (i) on-demand, in situ formation of microporous 3D constructs, (ii) pre-defined interconnected microporosity (regulated by microgel size and packing density), (iii) decoupled stiffness from porosity, and (iv) modular microarchitecture. Despite the recent advances in engineering microgel-based granular hydrogels for tissue engineering, additive manufacturing the granular hydrogels is not as trivial as bulk hydrogels. Microgels fabricated from various biomaterials, such as polyethylene glycol, chitosan, alginate, gelatin, and acrylic polymers, have been explored in bioinks, spheroid fabrication, and stimuli-responsive constructs. While bulk hydrogels may readily be rendered shear-thinning for extrusion-based bioprinting, granular hydrogels attain such rheological behavior only when they are in a “jammed” (tightly packed) state or embedded in a viscous matrix, which in turn compromises the void space among the microgels. Using large nozzles may improve the extrudability of granular hydrogels; however, achieving sub-mm resolution remains a bottleneck in the 3D bioprinting of granular microporous hydrogels.
Jamming in granular systems is defined as a physical process by which the viscosity increases as the volume fraction (φ) or particle number density increases. In other words, jamming signifies the transition of particulate systems from fluid-like to solid-like states, which varies in frictionless or frictional soft granular materials. In frictionless granules, jamming occurs beyond the state wherein particles are closely packed (Pc), i.e., ranging from 0.56 (random close-packed) to 0.74 (hexagonal close-packed) for monodispersed spheres. The jamming point is more complicated for frictional granules in which volume fraction is not the only indicator of jamming, and the jammed state may be reached at lower φ. Interaction between frictional microgels is an unexplored area in tuning the jamming, extrudability, and 3D bioprinting of granular systems. Confined microscale granules often undergo weak bonding among the adjacent particles via hydrogen bonding and/or electrostatic attraction. Such weak interactions enable the collective motion of microgels upon the exertion of sufficient pressure, enabling cohesive material flow through nozzles, followed by recovery after the backpressure is released. The microgels have to be jammed to maximize such weak interactions for enhanced printability, which inevitably minimize the void space among them.
Accordingly, there is currently an unmet need to develop granular bioinks that can preserve the microscale pores among microgels during and after extrusion bioprinting.
A generalized class of granular bioinks with remarkable extrusion printability, printing resolution, shape fidelity, and preserved interconnected microporosity have been produced. The microgel-microgel interactions may be engineered via the reversible interfacial self-assembly of heterogeneously charged nanoparticles. Embodiments may be based on the premise that dangling chains protruding out of polymeric microgels may adsorb the nanoparticles, followed by the charge-driven self-assembly of nanoparticles, imparting dynamic bonding to loosely packed microgels. Such dynamic bonds may form/break upon release/exertion of shear force, enabling the 3D printability of microgel suspensions without densely packing them. Embodiments may provide new opportunities for 3D bioprinting of tissues beyond the traditional biofabrication window.
In an exemplary embodiment, a method of forming a three-dimensional hydrogel scaffold comprises providing a granular bioink material comprising hydrogel particles, wherein the hydrogel particles are reversibly connected using a connection medium; extruding the bioink material; and exposing the extruded bioink material to a stimulus to form the three-dimensional hydrogel scaffold.
In some embodiments, the connection medium is nanoparticles.
In some embodiments, the hydrogel particles are selected from the group consisting of synthetic polymers, natural polymers, and/or semi natural polymers. In some embodiments, the hydrogel particles are gelatin methacryloyl.
In some embodiments, the step of providing the granular bioink material comprises forming gelatin methacryloyl by combining gelatin and methacrylic anhydride; forming the hydrogel particles by combining the gelatin methacryloyl and a photoinitiator; and combining the hydrogel particles with a connection medium, wherein the connection medium is nanoparticles.
In some embodiments, the photoinitiator is selected from the group consisting of lithium phenyl-2,4,6-trimethylbenzoylphosphinate, Ruthenium, and Irgacure 2959.
In some embodiments, the three-dimensional hydrogel scaffold comprises granular filaments with a diameter less than 400 μm.
In some embodiments, the stimulus is a light source with a wavelength of 250-785 nm. In some embodiments, the stimulus is a light source with a wavelength of 395-405 nm.
In some embodiments, the granular bioink material comprises silicate nanoparticles.
In an exemplary embodiment, a granular bioink material suitable for providing a three-dimensional hydrogel scaffold comprises gelatin methacryloyl hydrogel particles and a connection medium configured to reversibly connect the hydrogel particles.
In some embodiments, the connection medium is nanoparticles configured to be absorbed onto the hydrogel particles and wherein the nanoparticles are configured to allow for electrostatic bonding of the hydrogel particles.
In some embodiments, the nanoparticles are silicate nanoparticles.
In some embodiments, the nanoparticles are heterogeneously charged.
In some embodiments, the hydrogel particles have a size between 1 nm-1 mm.
In some embodiments, the hydrogel particles have an aspect ratio between 1-10.
In an exemplary embodiment, a three-dimensional hydrogel scaffold comprises a plurality of granular filaments, each filament comprising gelatin methacryloyl hydrogel particles and optionally nanoparticles.
In some embodiments, the filaments have a diameter less than 400 μm.
In some embodiments, the scaffold has a mean pore size of 1-1000 μm.
In some embodiments, the scaffold has a mean pore size of 10-100 μm.
In some embodiments, the scaffold has a minimum pore size of 100 nm.
In some embodiments, the scaffold has a minimum pore size of 10 μm.
In some embodiments, the scaffold has a void fraction of 10-40%.
Further features, aspects, objects, advantages, and possible applications of the present invention will become apparent from a study of the exemplary embodiments and examples described below, in combination with the Figures, and the appended claims.
The above and other objects, aspects, features, advantages, and possible applications of the present invention will be more apparent from the following more particular description thereof, presented in conjunction with the following drawings. It should be understood that like reference numbers used in the drawings may identify like components.
The following description is of an embodiment presently contemplated for carrying out the present invention. This description is not to be taken in a limiting sense but is made merely for the purpose of describing the general principles and features of the present invention. The scope of the present invention should be determined with reference to the claims.
It is contemplated that the terms “microgel” and “hydrogel particles” are used interchangeably throughout the present disclosure.
Referring to
It is contemplated that the hydrogel particles may be of any composition, including but not limited to gelatin methacryloyl, polyethylene glycol, hyaluronic acid, alginate, poly(N-isopropylacrylamide), polyacrylamide, or any combination thereof. In a preferred embodiment, the hydrogel particles are gelatin methacryloyl. It is further contemplated that the hydrogel particles may be of any shape, including but not limited to spherical, rod-like, disk-like, star-like, sheet-like, needle-like, irregularly shaped, porous, or any combination thereof. In a preferred embodiment, the hydrogel particles are spherical. It is further contemplated that the hydrogel particles may be of any size. In exemplary embodiments, the size of the hydrogel particles ranges from 1 nm-1 mm, preferably from 10-200 μm. It is further contemplated that the hydrogel particles may be of any aspect ratio. In exemplary embodiments, the aspect ratio of the hydrogel particles ranges from 0.01-100, preferably from 1-10.
In exemplary embodiments, the bio hydrogel particles may be formed using a photoinitiator. The photoinitiator may be selected from the group consisting of lithium phenyl-2,4,6-trimethylbenzoylphosphinate (LAP), Ruthenium, Irgacure 2959, or any other suitable photoinitiator.
In an embodiment wherein the hydrogel particles are gelatin methacryloyl, the gelatin methacryloyl may be formed by combining gelatin and methacrylic anhydride and optionally a photoinitiator. It is contemplated that any other synthetic, semi-synthetic/semi-natural, and natural polymer may be used to make the bioink.
Any microgel-microgel binding mechanism (e.g., connection medium) can be used to impart structural integrity to bioink before, during, or after 3D printing, e.g., nanoparticle self-assembly, photocrosslinking, dynamic covalent bond formation, any covalent bond formation, any physical interactions, such as ionic bonding and/or hydrogen bonding. In an embodiment wherein a connection medium is nanoparticles, it is contemplated that the nanoparticles may be absorbed onto the hydrogel particles and configured to allow for electrostatic bonding of the hydrogel particles. In particular, embodiments are based on the premise that dangling chains protruding out of the hydrogel particles may adsorb the nanoparticles, followed by the charge-driven self-assembly of nanoparticles, imparting dynamic bonding to loosely packed hydrogel particles. These dynamic bonds may form/break upon release/exertion of shear force, enabling the 3D printability of hydrogel suspensions without densely packing them.
In exemplary embodiments, the nanoparticles may be selected from the group consisting of silicate, clays, silica, mesoporous nanosilica, MXenes, and any other inorganic or organic particle that can induce reversible assembly of hydrogel particles. In a preferred embodiment, the nanoparticles are silicate nanoparticles. It is contemplated that the nanoparticles may be heterogeneously charged. In particular, the nanoparticles may be heterogeneous equipped with charged groups, which may readily absorb to a surface of the microgel and electrostatically bond to the charged groups on the exposed chains.
The method can involve extruding the granular bioink material, and exposing the extruded bioink material to a suitable stimulus to form the three-dimensional hydrogel scaffold. The stimulus may be selected from the group consisting of a light source, chemically generated free radical, temperature alteration, and reversible covalent and/or non-covalent bond formation. It is contemplated that the hydrogel scaffold may have favorable properties including, but not limited to, extrudability, printability, shape fidelity, and preserved interconnected porosity (e.g., ranging from 100 nm to 1000 μm, preferably 10-100 μm). In particular, it is contemplated that the hydrogel scaffold has a mean pore size of 1-1000 μm, preferably, 10-100 μm, a minimum pore size of 100 nm, preferably 10 μm, and a void fraction of 1-99%, preferably 10-40%.
To generate hydrogel particles, the building blocks of NGB bioink, a high-throughput step emulsification microfluidic device was microfabricated to produce>40 million droplets per hour.
GelMA and a photoinitiator were used as the aqueous (dispersed) phase, expanding in a continuous oil phase to form photocrosslinkable GelMA droplets. The droplets were collected and stored at low temperature (4° C.) to form thermally crosslinked GelMA microgels, which were separated from the oil phase after destabilizing the emulsion. The NGB was then formed by imparting interfacial reversible microgel-microgel bonding using silicate nanoparticles to enable the coherent extrusion of granular bioink through nozzles while preserving the interstitial void spaces among the hydrogel particles (
Hydrogel particles may readily be used to fabricate a variety of granular biomaterials with different extents of packing. To compare the NGB with commonly available granular systems, tightly or loosely packed hydrogel particle systems were fabricated by sequential centrifugation, as presented in
Jamming has recently been used to increase the contact area among hydrogel particles and enhance their extrudability/printability. However, maximizing the contact area of hydrogel particles results in minimizing the interstitial void spaces among them. Therefore, a tradeoff between extrudability/printability and pore availability arises, implying that to achieve decent printability, interconnected microscale pores are compromised.
Rheological behavior of bioinks regulate their extrudability, printability, and shape fidelity in extrusion-based bioprinting. The NGB was characterized using different rheological assessments to confirm its suitability for extrusion bioprinting.
The extrusion bioprinting of granular hydrogels was regulated by the microgel-microgel interactions during and after extrusion. Such interactions were maximized in jammed and matrix-embedded granules; however, maximizing the contact area of hydrogel particles or embedding them in a non-porous matrix compromised the microporosity. Surface-nanoengineered loosely packed hydrogel particles using shear-responsive nanoparticles that can reversibly self-assemble may enable strong microgel-microgel interactions, facilitating extrusion via micro-nozzles while preserving interconnected microscale pores among the hydrogel particles.
To test the hypothesis, molecular transport in different nano-/microporous scaffolds was assessed in
The scaffolds were exposed to FITC-dextran from the side (see
To quantify the interconnected porosity of NGB scaffolds, they were labeled using the FITC-dextran and 3D imaged.
Standard tapered bioprinting micro-nozzles were used at varying conditions to optimize the NGB extrusion bioprinting at the sub-mm resolution. Three nozzle opening IDs of 410, 250, and 200 μm, represented by blue, red, and clear nozzles, respectively, were used (
For each nozzle, there exists a minimum onset pressure to initiate the extrusion regardless of the printing speed. The smaller the nozzle opening, the higher the onset extrusion pressure. This is mainly a result of increased wall resistance in narrower channels. In a larger nozzle opening (i.e., blue nozzle, tip ID=410 μm,
Increasing the printing speed may result in discontinuous filaments at relatively low extrusion pressure. This condition is a result of a tradeoff between the amount of NGB dispensed from the tip and the contact time between the NGB and the substrate. As an example, for the blue (
Standard printability and shape fidelity assays were performed based on established protocols. For printability analysis, horizontal (0-degree) and vertical (90-degree) layers were custom-coded and deposited in two consecutive layers on top of each other, as shown in
NGB printability indices were measured by varying the nozzle opening. The printed structures were imaged using merged tile-scanned microscopy for the blue (
The relative evaluation of layer stacking in hollow cylinder models was performed to evaluate the shape fidelity. Cylinders with a base diameter and height of 5 mm were 3D bioprinted, as presented in
Mechanical and rheological properties of 3D bioprinted NGB scaffolds were evaluated using compression tests and oscillatory rheology, respectively. NGB scaffolds consisting of three bioprinted stacked layers were photocrosslinked using a light source (wavelength=395-405 nm, intensity=15 mW cm−2) (
The viscoelastic properties of 3D bioprinted NGB, molded NGB, and bulk GelMA scaffolds were analyzed using oscillatory rheology. First, the scaffolds underwent oscillatory amplitude sweep at a constant frequency (1 rad s−1) to determine the LVR, as presented in
In vitro analyses were performed on 3D bioprinted NGB scaffolds to assess post-printing, on-demand cell seeding and penetration, metabolic activity, and viability.
Overall, granular bioinks with well-preserved microscale porosity for the 3D extrusion bioprinting of tissue engineering scaffolds have been developed. Suspensions of otherwise non-extrudable loosely packed hydrogel particles have been rendered 3D bioprintable (NGB) via engineering the interparticle interactions based on the reversible interfacial self-assembly of heterogeneously charged nanoparticles. The NGB attains a shear-yielding behavior with prompt recovery, yielding higher hanging filament length, i.e., higher shape fidelity compared with tightly packed granular hydrogels. In addition, the NGB enables the sub-mm resolution extrusion bioprinting of granular scaffolds with cell-scale interconnected microporosity, ready to be 3D seeded with cells after printing. Considering the emerging interests of granular hydrogels for in situ tissue engineering, regeneration, and modeling, it is speculated that the unique, unprecedented properties of NGB, such as preserved porosity and maximized printability and shape fidelity, may enable a novel universal platform for the biofabrication of granular scaffolds.
High-throughput step emulsification microfluidic devices were fabricated via soft lithography in the Nanofabrication facilities of Materials Research Institute (MRI) at the Pennsylvania State University (Penn State) according to an established protocol. Master molds were fabricated using KMPR® 1000 series (Kayaku Advanced Materials, MA, USA) as negative photoresists on 4-inch mechanical grade silicon wafers (UniversityWafer, MA, USA). A Two-layer lithography process was performed with KMPR® 1025 and KMPR 1035 for the first and second layers, respectively. UV light exposure and alignment were performed by MA/BA6 (SÜSS MicroTeck, Germany) using designed alignment marks. UV exposure dose was set to 645 and 2000 mJ/cm2 for the first and second layers, respectively. Soft bake and post bake durations were adopted from the photoresist technical datasheet. The thickness of the first (27 μm) and second (140 μm) layers regulates the nozzle and reservoir height, respectively, which was measured using a profilometer (Tecncor P16+, KLA, CA, USA). The devices were molded on the masters using the polydimethylsiloxane (PDMS) Sylgard 184 kit (Dow Corning, MI, USA). The base and crosslinker were well-mixed at a 10:1 mass ratio, vacuum degassed, poured onto the masters, vacuum degassed again to remove all the air bubbles, and cured at 80° C. for 2 h. The PDMS devices were cut, plasma bonded to glass microscope slides (VWR, PA, USA), and placed in the oven to facilitate the bonding at 80° C. for 2 h.
GelMA was synthesized according to the following method. Gelatin (20 g, Type A from porcine skin, Sigma, MA, USA) was dissolved in 200 mL of Dulbecco's phosphate-buffered saline (DPBS) at 50° C. while stirring at 200 rpm. Then, 16 mL of methacrylic anhydride (MAA, Sigma, MA, USA) was added dropwise to the stirring solution at 50° C., and the reaction beaker was wrapped in aluminum foil to protect from light. After 2 h, the reaction was stopped by adding 400 mL of excess DPBS. The solution was dialyzed against ultra-pure Milli-Q® water (electrical resistivity≈18 MΩ at 25° C., Millipore Corporation, MA, USA) for 10 days at 40° C. using 12-14 kDa molecular weight cutoff (MWCO) membranes (Spectrum Laboratories, NJ, USA) to remove unreacted MAA. A clear solution was obtained, sterile filtered using a 0.20 μm vacuum filtration unit (VWR, PA, USA), and frozen at −80° C., followed by lyophilization to yield white GelMA solid.
The degree of methacrylate/methacryloyl substitution (DS) of GelMA was determined using 1H NMR (400 MHz Bruker NEO, MA, USA) at the NMR facilities of Penn State according to an established method. About 40 mg of gelatin powder and lyophilized GelMA were separately dissolved in 2 mL of deuterium oxide (D2O, Sigma, MO, USA) for 2 h at 37° C. The area was integrated using TopSpin 4.0.7 software considering the peaks of aromatic acids, which appeared at a chemical shift around 6.5-7.5 ppm as the reference. The lysine methylene proton peaks at a chemical shift around 3.0 ppm were used to determine the DS according to the following equation:
GelMA polymer was dissolved in Dulbecco's modified eagle medium (DMEM) or DPBS, including 0.1% w/v PI (lithium phenyl-2,4,6-trimethylbenzoylphosphinate, LAP, Sigma, MO, USA) at 50° C. to prepare a GelMA solution (10% w/v). The GelMA solution was used as the dispersed (aqueous) phase, and a mixture of Novec 7500™ engineering oil (3M, MN, USA), containing 2% v/v of a surfactant (Pico-Surf™, Sphere Fluidics, Cambridge, UK), was used as the continuous (oil) phase. The solutions were loaded into 5 mL syringes (BD, NJ, USA) and injected into the device using syringe pumps (PHD 2000, Harvard Apparatus, MA, USA) to form an emulsion of GelMA droplets in the oil. The droplet fabrication system was maintained at 35-40° C. using a space heater. The droplet suspension in oil was collected and stored at 4° C. overnight while protecting from light to obtain physically crosslinked GelMA microgels.
To prepare bulk (nonporous) hydrogel scaffolds, lyophilized GelMA was dissolved in DPBS containing 0.1% w/v of the PI at 50° C. to yield a clear GelMA solution (10% w/v). The GelMA solution was pipetted in laser-cut cylindrical acrylic molds with pre-warmed (50° C.) pipette tips (VWR, PA, USA), and place in a custom-built dark humidity chamber. The humidity chamber was a petri dish (100 mm, VWR, PA, USA) filled with wet paper towels to prevent drying, wrapped in aluminum foil to avoid light exposure. The molded GelMA solution was physically crosslinked inside the humidity chamber at 4° C. for 8 h, following by chemical photocrosslinking using light with a wavelength of 395-405 nm and intensity of 15 mW cm-2 for 60 s.
GelMA microgels in the oil were washed with 1H, 1H,2H,2H-perfluoro-1-octanol (PFO, 20% v/v in Novec 7500™ oil, Alfa Aesar, MA, USA) at a 1:1 volume ratio and centrifuged at 300×g for 15 s (including the ramp-up) to remove the surfactant and oil from the suspension. A PI solution (0.1% w/v in DPBS) was added to the washed microgel suspension and vortexed immediately for 5 s. Then, the suspension was centrifuged once at 2,940×g for 15 s or five times at 16,000×g for 60 s to yield loosely packed and tightly packed granular systems, respectively. Loosely packed microgel suspensions were pipetted out using a positive displacement pipette (Microman E M100E, Gilson, OH, USA) and injected into a cylindrical laser-cut acrylic mold (diameter=8 mm, height=3 mm). Tightly packed microgels were scooped out using a spatula and molded similarly. Then, the hydrogels were photocrosslinked via light exposure (wavelength=395-405 nm and intensity=15 mW cm−2) for 60 s to form microgel-microgel covalent bonds as a result of the free radical polymerization of GelMA vinyl groups.
To make the colloidal gel, silicate nanoparticles (LAPONITE® XLG nanoplatelets, BYK USA Inc., CT, USA) were exfoliated in cold Milli-Q® water at 4° C. Briefly, a nanoparticle dispersion (3% w/v) was prepared by adding 100 mg f LAPONITE® powder to 3.333 mL of Milli-Q® water at 4° C., followed by immediate vigorous vortexing for at least 15 min until a clear dispersion was obtained. The dispersion was maintained at 4° C. for at least 24 h to obtain aging-induced colloidal hydrogels.
A silicate nanoparticle dispersion (3.33% w/v) was prepared by adding 100 mg of LAPONITE® powder to 3 mL of Milli-Q® water, followed by exfoliation until a clear dispersion was obtained. From a stock solution of PI (LAP, 1.0% w/v in Milli-Q® water at 4° C.), 333 μL was added to the nanoparticle dispersion to obtain 3% w/v nanoparticle dispersion containing 0.1% w/v of the PI. In parallel, physically crosslinked GelMA microgel suspension in oil were washed with PFO (20% v/v in Novec 7500™ oil) at a 1:1 volume ratio and centrifuged at 300×g for 15 s (including the ramp-up) to remove the surfactant and oil from the suspension at 4° C. The silicate nanoparticle dispersion was then added to the microgel suspension and vortexed immediately for 15 s to ensure that the microgels and nanoparticles were well mixed. The resulting suspension was then centrifuged at 2,940×g for 15 s (including ramp-up), the supernatant was removed, and the microgel nanocomposite was aged for 1 day at 4° C. to form the NGB. The NGB was loaded into Luer-Lock syringes (3 mL, BD, NJ, USA), pulse centrifuged at 300×g to remove trapped air, and maintained at 4° C. while covered with aluminum foil to protect from light for further analyses or 3D bioprinting.
To characterize the rheological properties of NGB, an AR-G2 Rheometer (TA instrument, DE, USA) equipped with parallel plates (upper plate diameter=20 mm and truncation gap=1000 μm). The lower plate temperature was set to 4° C., the NGB was loaded on it, sandwiched by the upper plate, and its excess amount was trimmed. The rheological behavior of NGB was characterized by several tests, including: (i) steady shear rate sweep, where the shear rate was altered from 10−2 to 102 s−1, (ii) oscillatory strain sweep at strain of 10−2 to 5×102% and a constant oscillation frequency of 1 rad s−1, (iii) oscillatory frequency sweep at 10−2 to 102 rad s−1 and constant strain of 0.1%, (iv) a recovery test, performed by alternating the strain between 1% and 500% over time at a constant frequency of 1 rad s−1, and (v) time sweep, which was performed on freshly prepared (non-aged) NGB at a constant frequency of 1 rad s−1 and strain of 0.1% over time for 4 h.
To assess the pore availability and interconnectivity, bulk (nanoporous) and granular hydrogels were examined. Bulk GelMA (10% w/v) was prepared in DPBS containing 0.1% PI at 37° C. Colloidal gel, tightly packed, and loosely packed systems were prepared as previously described. All materials except the bioink were casted in a cylinder with a diameter of 8 mm and height of 3 mm. The NGB was 3D bioprinted in a similar shape. Samples were placed in a custom-developed PDMS mold (
Compression tests were performed on the hydrogel scaffolds photocrosslinked as cylindrical specimen (diameter=8 mm, height=1 mm) using the Instron mechanical tester (Instron 5542, MA, USA). The compression rate was 1 mm min−1, and stress versus strain curves were obtained. The best linear fit at the elastic region (strain˜5%-15%) was obtained, and the slope was reported as the compressive modulus. For viscoelasticity analysis, cylindrical hydrogel samples (diameter=8 mm, height=1 mm) were prepared. Oscillatory shear rheology was performed using the rheometer at 25° C. The top and bottom plates were 8 mm and 25 mm, respectively. The storage and loss moduli were recorded first based on amplitude sweep for furnishing linear viscoelastic region (LVR) at a fixed frequency (1 rad s−1) from 0.1 to 100% of strain, and then 637 based on frequency sweep at 0.1% of strain (in the LVR) from 0.1 to 100 rad s−1.
To measure the maximum hanging filament length, mechanical extrusion of NGB, tightly packed, and loosely packed granular hydrogels was conducted using the Instron mechanical tester (Instron 5542, MA, USA). Samples were loaded in 3 mL syringes (BD, NJ, USA). Blue (22G), red (25G), and clear (27G) nozzles with an inner diameter of 410, 250, and 200 μm, respectively, were used. The injection rate was 4.25 mm min-1 (flow rate=250 AL min−1). Extruded filaments were recorded using a Canon SX700HS camera and analyzed using the ImageJ software (FIJI, version 1.53n, NIH, MD, USA)
Molded and 3D bioprinted hydrogel samples were incubated in a high molecular weight FITC-dextran solution (Mw˜2 MDa, 15 μM in Milli-Q® water) for 30 min to fill the void spaces among the microgels with the dye. Pore size distribution and void fraction were analyzed using 3D z-stacked images acquired using the Leica DMi8 THUNDER™ microscope. One hundred z-stacks were captured for each sample, covering a total depth of 140 μm. The void fraction was measured using the built-in microscope software (LAS X 5.0.3 Life Science Microscope Software Platform) based on the ratio of stained interstitial space over total volume. Microporosity was characterized using a custom-built computer code (MATLAB, version 2021b) as previously described. For the median pore diameter, the equivalent diameter of detected pores was measured based on circles of similar area, followed by calculating the median value for each sample.
NGB was 3D bioprinted using a BIO X bioprinter (Cellink, MA, USA). To conduct bioprinting, the bioink was loaded in 3 mL cartridges (Cellink, MA, USA) using a female-female Luer-Lok™ connector, pulse centrifuged at 200×g to eliminate air bubbles, wrapped in aluminum foil to protect from light, and maintained at 4° C. The printing bed temperature was set to 4° C., and the printed structures were exposed to light (wavelength=395-405 nm, intensity=15 mW/cm2) for up to 4 min, depending on the sample thickness.
For printability quantification, two consecutive layers of NGB were printed on top of each other. Printed constructs followed horizontal or vertical (0 or) 90° printing of 15 mm parallel lines pattern with increasing distance between adjacent filaments according to an established method. The printing window was deposited using a custom-developed G-code file, ranging from 1×1 to 5×5 mm2 with 1 mm increments. Digital single-lens reflex (DSLR) and tile scan microscopic images of printed constructs were taken right after the fabrication by a Canon SX700HS camera and Leica DMi8 microscope, respectively. The images are analyzed using ImageJ software by inverting, thresholding, and analyzing particles (
The standard shape fidelity test was performed by 3D bioprinting a hollow cylindrical structure with a diameter of 5 mm and height of 5 or 10 mm. The deposited layer numbers ranged from 12 to 50 depending on the filament size and the cylinder height. For the 5 mm high cylinder, the number of layers were 12, 20, and 25 for the 22G, 25G, and 27G nozzles, respectively. In addition, for the longer, 10 mm high cylinder, the number of layers were 24, 40, and 50 for the 22G, 25G, and 27G nozzles, respectively. The DSLR images of 3D bioprinted structures were captured by a Canon SX700HS camera, and measurements were performed using the ImageJ software. The height collapse factor was measured as the ratio of actual (Ha) height to the theoretical (Ht) height, as described in the following equation:
NIH/3T3 murine fibroblast cells (ATCC, VA, USA) were cultured in DMEM, supplemented with 10% v/v fetal bovine serum and 1% v/v antibiotic. The media was refreshed every other day, and the cells were passaged when they reached 80% of confluency, typically twice per week. A standard cell culture incubator (Eppendorf, Hamburg, Germany) was used to culture cells in T-75 cell culture flasks (VWR, PA, USA) under a 5% v/v CO2 atmosphere at 37° C. Fibroblasts were trypsinized using 0.25% trypsin-EDTA (Sigma, MO, USA), followed by cell counting using an automated cell counter device (Countess 2, Thermo Fisher Scientific, MA, USA) and resuspension in the media for 3D topical cell seeding.
Topical cell seeding in the 3D bioprinted NGB scaffolds was performed to evaluate cell penetration and viability. The NGB scaffolds were 3D bioprinted and soaked in DPBS supplemented with 1% v/v antibiotic overnight. Then the scaffolds were placed in a non-treated 48-well cell culture plate (Cellstar®, Greiner Bio-One, Austria) filled with DBPS. DPBS was then discarded, and 20 μL of the cell suspension containing 5 million cells per mL was added on top of each scaffold. The scaffolds were incubated for 30 min to ensure cell-scaffold adhesion, followed by adding the complete cell culture media. The seeded scaffolds were incubated, and the media was refreshed daily.
PrestoBlue™ cell viability kit (Invitrogen, MA, USA) was used to evaluate the cellular metabolic activity on days 1, 4, and 7 based on the manufacturer protocol. PrestoBlue was mixed with DMEM in a 1:10 v/v ratio to make a 1× solution. For each cell-seeded scaffold, 500 μL of PrestoBlue 1× solution was added to the well and incubated for 4 h at 37° C. The supernatant was removed and poured into 96-well plates (Cellstar®, Greiner Bio-One, Austria). Fluorescence intensity was recorded using a microplate reader (Tecan Infinite M Plex, Männedorf, Switzerland) at 530 nm excitation and 590 nm emission and corrected with respect to the background signal of the virgin PrestoBlue media.
Two-color fluorescence Live/Dead cell viability assay kit (Invitrogen, MA, USA) was used according to the manufacturer protocol to evaluate the cell viability of seeded scaffolds. Calcein AM (1 mL, 1 μM) was used for staining live cells, while BOBO™-3 Iodide (1 μL) was used as a dead cell indicator. The samples were incubated at 20° C. for 15 minutes and imaged using the Leica DMi8 fluorescent microscope. The live channel was set at 470 nm (blue) excitation and 510 nm (green) emission wavelengths. The dead channel was set to 550 nm (green) excitation and 610 nm (red) emission wavelengths.
Data was acquired with at least three iterations. For the analysis of significance, the one-way analysis of variance (ANOVA) test was carried out, followed by the Tukey and Bonferroni post hoc tests. Groups were considered significantly different if the p-value was lower than 0.05. The level of significance was noted with *p<0.05, **p<0.01, and *** p<0.001.
Each of the following references is incorporated herein by reference in its entirety.
It should be understood that the disclosure of a range of values is a disclosure of every numerical value within that range, including the end points. It should also be appreciated that some components, features, and/or configurations may be described in connection with only one particular embodiment, but these same components, features, and/or configurations can be applied or used with many other embodiments and should be considered applicable to the other embodiments, unless stated otherwise or unless such a component, feature, and/or configuration is technically impossible to use with the other embodiment. Thus, the components, features, and/or configurations of the various embodiments can be combined together in any manner and such combinations are expressly contemplated and disclosed by this statement.
It will be apparent to those skilled in the art that numerous modifications and variations of the described examples and embodiments are possible considering the above teachings of the disclosure. The disclosed examples and embodiments are presented for purposes of illustration only. Other alternate embodiments may include some or all of the features disclosed herein. Therefore, it is the intent to cover all such modifications and alternate embodiments as may come within the true scope of this invention, which is to be given the full breadth thereof.
It should be understood that modifications to the embodiments disclosed herein can be made to meet a particular set of design criteria. Therefore, while certain exemplary embodiments of the apparatus and methods of using and making the same disclosed herein have been discussed and illustrated, it is to be distinctly understood that the invention is not limited thereto but may be otherwise variously embodied and practiced within the scope of the following claims.
This patent application is related to and claims the benefit of priority of U.S. provisional application 63/324,774, filed on Mar. 29, 2022, the entire contents of which is incorporated by reference, and is further related to and claims the benefit of priority of U.S. provisional application 63/367,521, filed on Jul. 1, 2022, the entire contents of which is incorporated by reference, and is further related to and claims the benefit of priority of U.S. provisional application 63/424,286, filed on Nov. 10, 2022, the entire contents of which is incorporated by reference.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2023/016651 | 3/29/2023 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 63324774 | Mar 2022 | US | |
| 63367521 | Jul 2022 | US | |
| 63424286 | Nov 2022 | US |