Patent Application
20180290380
The present disclosure relates to a method for continuously forming a three-dimensional body from a mixture, the mixture comprising solid particles and a radiation curable material.
The manufacturing of polymeric three-dimensional bodies based on a layer by layer built up of a radiation curable liquid material has become of increasing interest, especially in view of the enhancement in production speed if a bottom-up technique is employed.
Although it is known that ceramic bodies may also be manufactured via a layer by layer construction of radiation curable ceramic slurries, the production speed for making these materials is still very slow and improvement of the uniformity, density and strength of manufactured ceramic bodies is desirable. The manufacturing of complex three dimensional structures including ceramic can find applications in a wide range of fields, for example, in the automotive and aerospace industry, or in medicine for the making of custom implants and dental models.
According to one embodiment, a method of forming a body comprises forming a three-dimensional body from a mixture, the mixture comprising at least 15 vol % of solid particles for a total volume of the mixture and a radiation-curable material, wherein forming includes continuous translation and growth of the body from an interface of the mixture.
According to another embodiment, a method of forming a body comprises providing an assembly including a chamber containing a mixture and a construction; forming a three-dimensional body by continuously creating and attaching a radiation cured translating portion to a carrier plate of the construction and increasing a distance between the carrier plate and the mixture in a continuous manner to create a three-dimensional body within the mixture, wherein during forming the three-dimensional body is adjacent to an interface of an inhibition zone of the mixture. The mixture comprises a mixture characteristic selected from the group of a shear-thinning slurry; a shear-thinning slurry with a radiation-curable material; a content of solid particles of at least 15 vol % for a total volume of the mixture; a yield point of less than 10 Pa; a viscosity of at least 50 cP at a shear rate of less than about 5 Hz, and a viscosity of less than 1000 cP at a shear rate greater than about 25 Hz; or a combination thereof.
According to a further embodiment, a method of forming a body comprises forming a three-dimensional body using an additive manufacturing process, the three-dimensional body having a content of ceramic particles of at least 15 vol % for a total volume of the three-dimensional body, wherein the three-dimensional body has a total volume of at least 0.1 mm3, and wherein creating is completed at a rate of at least 25 mm/hr.
The present disclosure may be better understood, and its numerous features and advantages made apparent to those skilled in the art by referencing the accompanying drawings.
As used herein, the terms “comprises,” “comprising,” “includes,” “including,” “has,” “having” or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a process, method, article, or apparatus that comprises a list of features is not necessarily limited only to those features but may include other features not expressly listed or inherent to such process, method, article, or apparatus.
As used herein, and unless expressly stated to the contrary, “or” refers to an inclusive-or and not to an exclusive-or. For example, a condition A or B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present), and both A and B are true (or present).
Also, the use of “a” or “an” are employed to describe elements and components described herein. This is done merely for convenience and to give a general sense of the scope of the invention. This description should be read to include one or at least one and the singular also includes the plural unless it is obvious that it is meant otherwise.
As used herein, the term mixture refers to a fluid of a certain viscosity, including a liquid component and solid particles. The liquid component may include a radiation curable material.
As used herein, the term three dimensional body refers to a body containing radiation cured resin and at least 15 vol % solid particles based on the total volume of three dimensional body. In the embodiments that the solid particles are ceramic particles, the three dimensional body is also called green body as a synonymous expression, as long it is before the stage of high temperature sintering (before removal of the cured resin).
Various embodiments of the present disclosure will now be described, by way of example only, with reference to the accompanying drawings.
The present disclosure relates to a method of continuously forming a three-dimensional body from a mixture. The mixture can comprise solid particles in an amount of at least 15 vol % and a liquid radiation-curable material, wherein the forming includes continuous translation and growth of the three-dimensional body from an interface of the mixture.
The method includes providing an assembly designed for working with radiation curable mixtures containing a particular concentration of solid particles. As demonstrated in the embodiment shown in
According to one embodiment, a carrier plate (18) can be positioned above the chamber (12). The position between the carrier plate (18) and the mixture in the chamber (12) can be changed during the forming process to facilitate formation of the three-dimensional body. When the formation of the three-dimensional body is started, the carrier plate (18) can be emerged into the mixture (16) up to a pre-calculated distance from the interface of the inhibition zone (22). According to one embodiment, the pre-calculated distance corresponds to a portion of the mixture that can be radiation cured (translated from liquid to solid state) if subjected to electromagnetic radiation from the radiation unit (11) underneath the chamber (12), and is furtheron called “translating portion” (19). The radiation cured translating portion (19) can adhere to the carrier plate (18) and be vertically moved away from the interface of the inhibition zone (22). Concurrently with the upwards movements of the carrier plate (18) and the attached solidified translating portion (19), mixture (16) from the sides of the polymerization chamber or from a reservoir (20) can fill the released space. The construction is designed to move the carrier plate (18) continuously upwards in z direction at a speed that corresponds to the time needed for radiation curing mixture (16) that replaces the upwards moved solidified translating portion.
The increase in distance between the carrier plate (18) and the mixture (16) when forming the three-dimensional body (21) can be caused by moving either the carrier plate (18) or the chamber (12) or both carrier plate (18) and chamber (12) in relation to each other.
The carrier plate (18) of the assembly of the present disclosure is configured for continuous movement to facilitate formation of the three-dimensional body away from the interface of the inhibition zone (22). As used herein, the phrase “interphase of the inhibition zone” (22) can be used interchangeable with the phrase “interface of the mixture,” since the inhibition zone is a zone of the mixture, which only distinguishes from the other part of the mixture by the presence of an inhibitor in a concentration that the mixture may not cure if exposed to electromagnetic radiation. Actual solidification and forming of the three dimensional body starts at the interface of the inhibition zone (22), i.e., an interface of the mixture.
The formation of the three dimensional body may not necessarily be considered a layer-by-layer forming process. Instead, the forming process (e.g., curing) may be in the form of a gradient of solidification (e.g., polymerization). The processes of the embodiments herein may facilitate formation of a three-dimensional body having smoother features and may have improved mechanical properties, compared to conventional structures formed by layer-by-layer forming processes.
As used in the context of the present disclosure, continuous translation and growth of the three-dimensional body means that the carrier plate (18) can be moved in a continuous manner or in discrete steps with short stops between each step, as long the stops allow that a gradient of solidification is maintained while forming the three-dimensional body. A gradient of solidification means that especially in the translating portion (19) a continuous polymerization reaction is maintained, with the highest degree of solidification at the farthest distance to the inhibition zone. The three-dimensional body formed by the process of continuous translation can thereby possess a non-layered internal structure, such that in a crosscut along the z-axis, changes in the morphology of the green body are not visible to the naked eye. In comparison, traditional layer by layer build-up of a green body waits until one layer is completely radiation cured before the next layer is applied, which leaves visible cleavage lines in the formed green body, i.e., regions that are not smoothly connected together.
In embodiments, the stops in the movement of the carrier plate (18) while conducting continuous translation and forming of the three-dimensional body can be at least 1 microsecond, such as at least 300 microseconds, at least 500 microseconds, at least 800 microseconds, or at least 1000 microseconds. In other embodiments, the stops during continuous translation may be not longer that 1 second, such as not longer than 0.5 seconds, not longer than 0.3 seconds, not longer than 0.2 seconds, or not longer than 0.1 seconds. It will be appreciated that the stops during continuous translation can be a value within any of the minimum and maximum values note above, such as from 1 microsecond to 1 second, from 300 microseconds to 0.5 seconds, or from 1000 microseconds to 0.1 seconds.
In further embodiments, the method of the present disclosure can also include one or more longer stops during the forming of the three-dimensional body, such that the gradient of solidification may be interrupted and the translation is not continuous as defined above. Such longer stops may be desired for the making of a body having defined regions which are cleavable.
The cure depth of the electromagnetic radiation (14) applied to the mixture (16) may be effected by the size, type, and concentration of the solid particles and the refractive index of the particle slurry. Notably, the size and concentration of the solid particles may be particularly selected to facilitate proper operation of the process in combination with the type of electromagnetic radiation used for the curing process.
According to an embodiment, suitable formation of a three-dimensional body having a suitable strength, can include controlling the cure depth relative to a thickness of the translating portion. In one embodiment, the cure depth may be at least 25% larger than the thickness of the translating portion (19), such as at least 30%, at least 35%, or at least 40%. In another embodiment, the cure depth can be not greater than 75% of the thickness of the translating portion (19), such as not greater than 70% or not greater than 65%. It will be appreciated that the cure depth can be a value between any of the maximum and minimum values noted above, such as from 25% to 75%, from 30% to 70% or from 35% to 60% of the thickness of the translating portion (19).
In one embodiment, a thickness of the translating portion (19) can be at least 50 μm, such as at least 70 μm, or at least 100 μm. In another embodiment, the thickness of the translating portion may be not greater than 500 μm, such as not greater than 450 μm, or not greater than 400 μm. It will be appreciated that the thickness of the translating portion can be a value between any of the maximum and minimum values note above, such as from 50 μm to 500 μm, from 80 μm to 450 μm, or from 100 μm to 300 μm.
In a further aspect, the cure depth may be at least 1 μm larger than the thickness of the inhibition zone (17), such as at least 5 μm, at least 10 μm, at least 20 μm, or at least 50 μm larger than the thickness of the inhibition zone. In yet another aspect, the cure depth can be not greater than 400 μm than the thickness of the inhibition zone, such as not greater than 350 μm, not greater than 300 μm, or not greater than 250 μm than the thickness of the inhibition zone. It will be appreciated that the cure depth can be a value between any of the maximum and minimum values noted above, such as within a range of at least 1 μm to not greater than 400 μm, from 5 μm to 370 μm, or from 30 μm to 300 μm larger than the thickness of the inhibition zone.
The thickness of the inhibition zone (17), which can be formed when the inhibitor enters the chamber (12) through the transparent and semipermeable window, (15) may be regulated by the concentration of the inhibitor. The inhibition zone (17) may limit the curing of the mixture (16) in that zone within the chamber (12). The inhibition zone (17) may facilitate limited or no adhesion of the radiation cured material to the bottom of the chamber (12), which may further facilitate simpler release of the body from the chamber after forming is completed.
In one embodiment, the thickness of the semipermeable layer for the penetration of inhibitor gas can be at least about 1 μm, such as at least about 5 μm, at least about 50 μm, at least about 500 μm, or at least about 1000 μm. The upper thickness of the semipermeable layer may not be limited as long the layer allows sufficient transport of inhibitor gas.
The material of the semipermeable layer may be any material that permits the penetration of inhibitor gas. Non-limiting examples of materials suitable for a semipermeable layer can include, for example, fluoropolymers, such as Teflon (e.g., AF-2400X), polymethylpentene based membranes (PMP), or silicone polymers and copolymers.
The inhibitor may preferably be an oxygen containing gas, such as air, mixtures of an inert gas and oxygen, or pure oxygen. In another aspect, when oxygen cannot inhibit the activity of the photoinitiator (for example, when a cationic photoinitiator is used) the inhibitor can be an amine, e.g., ammonia, ethyl amine, di and trialkyl amines, carbon dioxide, or combinations thereof.
In one embodiment, the inhibitor can be pure oxygen, and the oxygen may penetrate the semipermeable layer in an amount of at least 0.1 Barrer, such as at least 1 Barrer, at least 5 Barrer, at least 10 Barrer, or at least 30 Barrer.
The thickness of the inhibition zone should be at least in the range of the average size of the solid particles contained in the mixture or greater. In one embodiment, the thickness of the inhibition zone may be at least 0.5 μm, such as at least 1.0 μm, at least 2.0 μm, or at least 5 μm. In another embodiment, the inhibition zone may not be greater than 600 μm, such as not greater than 500 μm, not greater than 300 μm, or not greater than 100 μm. It will be appreciated that the thickness of the inhibition zone can be a value between any of the maximum and minimum values noted above, such as from 0.5 μm to 600 μm, from 1.0 μm to 450 μm, or from 3 μm to 200 μm.
Although the term “inhibition zone” appears to indicate that no polymerization reaction may take place in that area of the mixture, it will be appreciated that polymerization reactions can also occur to a limited extent in the inhibition zone. The inhibition zone may be also described as a gradient of polymerization, where with increasing distance from the bottom surface of the chamber larger amounts of polymerization reactions can happen, but these polymerization reactions may not completely cure the mixture, and the mixture is still maintained in a liquid stage. The interface of the inhibition zone may be understood as the area of the inhibition zone where the polymerization reactions start to form a solid material.
The solid particles contained in the mixture can be any type of inorganic or organic particles that do not dissolve in the liquid component of the mixture under the forming conditions, and may be uniformly distributed throughout the entire mixture. In one aspect, the solid particles can be ceramic particles, metallic particles, polymeric particles, or any combination thereof.
In a particular embodiment, the solid particles can be ceramic particles, such as an oxide, a carbide, a boride, a nitride, a silicide or any combination thereof. Non-limiting examples or ceramic particles can be alumina, ceria, zirconia, silica, magnesium-magnesia aluminate (MMA), magnesium oxide, silicon nitride, silicon carbide, hydroxyapatite, cordierite, or any combination thereof. In a particular embodiment, the ceramic particles are alumina, silica, MMA, or zirconia.
The concentration of the solid particles in the mixture can be in a range that a percolated network be formed and that the created three-dimensional body can be densified without falling apart upon burnout of the binder. In one embodiment, the concentration of solid particles can be at least 15 vol %, such as at least 16 vol %, at least 18 vol %, at least 20 vol %, at least 25 vol %, or at least 30 vol %. In another embodiment, the particle concentration can be not greater than 80 vol %, such as not greater than 75 vol %, not greater than 70 vol %, or not greater than 65 vol %. It will be appreciated that the concentration of solid particles can be a value between any of the maximum and minimum values noted above, such as from 16 vol % to 80 vol %, from 20 vol % to 75 vol %, or from 30 vol % to 65 vol %.
The solid particles contained in the mixture can have an average particle size of at least 0.1 μm, such as at least 0.5 μm, at least 1.0 μm, or at least 5 μm. In another aspect, the solid particles can have an average particle size of not greater than 20 μm, such as not greater than 18 μm, or not greater than 15 μm. It will be appreciated that the average size of the solid particles can be a value between any of the maximum and minimum values noted above, such as from 0.1 μm to 20 μm, 0.3 μm to 18 μm, or 0.5 μm to 15 μm.
In one embodiment, the solid particles may have a multimodal particle distribution, for example, a bimodal or trimodal particle distribution.
In order to provide a high quality of the formed three-dimensional body of the present disclosure, it can be advantageous if solid particles that exceed a certain particle size or particles that have a size below a certain minimum be excluded. In one embodiment, the solid particles may have a particle size distribution wherein a value of function (d50−d10)/d50 is less than 0.8. In another embodiment, the solid particles may have a particle size distribution wherein a value of function (d90−d50)/d50 is less than 1.0.
In another embodiment, the solid particles contained of the mixture may have an average particle size controlled relative to the thickness dimension of the inhibition zone. In a preferred aspect, an average particle size of the solid particles may not be greater than 25% of the thickness of the inhibition zone, such as not greater than 20%, not greater than 15%, or not greater than 10% of the thickness of the inhibition zone.
In one embodiment, the mixture can contain at least 20 vol % to 40 vol % ceramic particles and may be radiation cured with UV radiation having an energy of at least 30 mJ/cm2 and not greater than 200 mJ/cm2.
The radiation curable material contained in the mixture can comprise polymerizable monomers, polymerizable oligomers and one or more photoinitiators. In a preferred aspect, the radiation curable material can contain polymerizable monomers and at least one photoinitiator. Suitable polymerizable monomers can be, for example, acrylates, acrylamides, urethanes, dienes, or combinations thereof.
The photoinitiator can be a free-radical photoinitiator or a cationic photoinitiator. In a preferred aspect, a free-radical photoinitiator can be employed, which can be inhibited by the presence of oxygen. Non-limiting examples of free-radical photoinitiators can include peroxides, such as acetyl, benzoyl, t-butyl peroxides, ketones or phosphine oxides, such as IRGACURE 819 (bis(2,4,6-trimethylbenzoyl)-phenylphosphineoxide), ESSTECH TPO (2,4,6-trimethylbenzoyl)-phenylphosphineoxide) or a combination thereof.
In an embodiment where a cationic photoinitiator is used, the photopolymerization generally tends to be slower and cannot be inhibited by oxygen. In this aspect, instead of oxygen as inhibitor, a Bronsted acid or Lewis acid, such as metal halides and their organometallic derivatives can be employed and released from the bottom window of the polymerization chamber to form an inhibition zone.
The mixture comprising the solid particles and the radiation curable material can be subjected to electromagnetic radiation having a wavelength in a range from 200 nm to 760 nm, depending from the activation energy of the selected photoinitiator. In a preferred aspect, the range of the electromagnetic radiation may be from 370 nm to 450 nm, or from 380 nm to 410 nm.
In embodiments, the electromagnetic radiation can be created by a laser, a light emitting diode (led), or by electron beam radiation.
In one embodiment, the electromagnetic radiation applied for curing the mixture can have an energy of at least 20 mJ/cm2, such as at least 30 mJ/cm2, at least 50 mJ/cm2 or at least 80 mJ/cm2. In another embodiment, the electromagnetic radiation can have an energy not greater than 450 mJ/cm2, such as not greater than 400 mJ/cm2, not greater than 350 mJ/cm2, not greater than 300 mJ/cm2, not greater than 250 mJ/cm2, not greater than 200 mJ/cm2, or not greater than 100 mJ/cm2. It will be appreciated that the electromagnetic radiation energy can be a value between any of the maximum and minimum values noted above, such as from 20 mJ/cm2 to 450 mJ/cm2, from 30 mJ/cm2 to 300 mJ/cm2, from 40 mJ/cm2 to 200 mJ/cm2, or from 20 to 100 mJ/cm2.
In a particular embodiment, the method of the present disclosure may cure the mixture in the translation portion (19) during continuous forming of the three dimensional body at a UV power of at least 0.1 mW/cm2, such as at least 0.5 mW/cm2, at least 1.0 mW/cm2, or at least 3.0 mW/cm2. In another particular embodiment, the applied UV power during forming may be not greater than 250 mW/cm2, such as not greater than 150 mW/cm2, not greater than 100 mW/cm2, not greater than 50 mW/cm2, not greater than 30 mW/cm2, not greater than 20 mW/cm2, not greater than 13.0 mW/cm2, not greater than 12 mW/cm2, or not greater than 10 mW/cm2. It will be appreciated that the applied UV power can be a value between any of the maximum and minimum values noted above, such as from 0.1 mW/cm2 to 250.0 mW/cm2, from 1.0 mW/cm2 to 100 mW/cm2 or from 2.0 mW/cm2 to 10 mW/cm2.
In a further embodiment, the thickness dimension of the inhibition zone can be controlled relative to the concentration of the solid particles. By increasing the concentration of the solid particles, the thickness of the inhibition zone may be decreased, as also shown in Example 2.
In another embodiment, the solid particles contained in the mixture can include a coating overlying an exterior surface of the particles. The coating can partially or completely cover the surface of the solid particles. The coating may be desirable in order to adjust the scattering and/or absorption of an applied electromagnetic radiation in the mixture. In one aspect, the coating can provide a 50% lower scattering of an applied electromagnetic radiation than corresponding uncoated particles. In a further aspect, the coating can lower the radiation scattering by at least 55%, such as at least 60%, at least 70%, at least 80%, at least 90% or at least 95%.
In another aspect, a coating of the solid particles can provide a 50% lower absorbance of an applied electromagnetic radiation absorption than corresponding uncoated particles. In embodiments, the coating can lower the radiation absorbance in the mixture by at least 55%, such as at least 60%, at least 65%, at least 70%, at least 75%, at least 80%, at least 90% or at least 95%.
According to another embodiment of the present disclosure, the mixture may include one or more additives. Non-limiting examples of additives can be additional inhibitors to prevent spontaneous polymerization (inert dyes), plasticizer, dispersing agents, debinding accelerators, cross-linking monomers, pH regulators, a pharmaceutically active ingredient, or any combination thereof.
The rheological properties of the mixture containing solid particles and a radiation curable material may be controlled to facilitate suitable formation of a stable and suitably formed three-dimensional body, including for example, a ceramic green body having sufficient strength to be self-supporting and capable of handling without detrimental deformation. Also, the force required to continuously pull-up the carrier the force utilized to pull the carrier plate away from the chamber may be adjusted based on various parameters, including but not limited to the rheology of the mixture.
In a particular embodiment, the mixture used for forming the three dimensional body according to the present disclosure can be characterized that the viscosity of the mixture decreases with increasing shear rate. Such type of mixture is also called herein a shear thinning slurry. In certain embodiments, the decrease of the viscosity of the mixture from a shear rate of 0.1 s−1 to a shear rate of 500 s−1 can be at least 10 cP, such as at least 30 cP, at least 50 cP, or at least 80 cP. In other embodiments, the decrease in viscosity from a shear rate of 0.1 s−1 to a shear rate of 500 s−1 may be not greater than 1500 cP, such as not greater than 1200 cP, not greater than 1000 cP, or not greater than 800 cP. It will be appreciated that the decrease in viscosity from a shear rate of 0.1 s−1 to a shear rate of 500 s−1 may be a value within any of the maximum and minimum values noted above, such as from 10 cP to 1500 cP, from 50 cP to 700 cP, or from 10 cP to 100 cP.
In another aspect, the yield point of the mixture may be less than 10 Pa, such as less than 8 Pa, less than 5 Pa, or less than 3 Pa at room temperature.
In a further aspect, the mixture may have a low shear viscosity to prevent particle settling over the duration of the forming of the three-dimensional body. Furthermore, the solid particles contained in the slurry may be uniformly dispersed throughout the radiation curable material when electromagnetic radiation is conducted such that that the three-dimensional body can shrink uniformly during sintering. Non-uniform distribution of the solid particles may result in undesirable macro-structural or micro-structural features, including for example, undesirable porosity and the like. Under low shear rate may be understood a range of not greater about 5 Hz and at least about 0.001 Hz, with a corresponding viscosity from at least about 50 cP to not greater than about 5000 cP, particularly from at least 70 cP to not greater than 1500 cP. In one aspect, the viscosity at a low shear rate of less than about 5 Hz can be at least 100 cP.
The viscosity at a moderate to high shear rate can enable sufficient spontaneous flow of the mixture between carrier plate and the bottom surface of the polymerization chamber. Under moderate to high shear rate may be understood a shear rate in a range from at least about 25 Hz and not greater than about 3000 Hz, with a corresponding viscosity of the mixture in a range of at least 1 cP and not greater than 1000 cP. In one aspect, the viscosity of the mixture at a moderate to high shear rate of greater than 25 Hz may be less than 1000 cP.
In one embodiment, the mixture may be formed such that the content of agglomerates of the solid particles is limited. In certain embodiments, the mixture can be essentially free of agglomerates of solid particles. Forming a mixture that has limited agglomerates can include heat treatment and milling of the solid particle powder before combining with the other components of the mixture. In embodiments, the solid particle powder can be heat treated at least 90° C., such as at least 100° C. or even at least 105° C.
Other mixing methods may be employed. The mixing process may be controlled to control the level of agglomeration. Moreover, over-mixing may result in degrading of the monomers and generating too much premature polymerization of the radiation curable resin.
In one particular embodiment, the mixture can comprise alumina particles having an average particle size from 100 nm to 5000 nm in an amount of 15 vol % to 50 vol %.
In a certain embodiment, the alumina particles can have an average particle size from 300 nm to 3000 nm and may be present in an amount of 18 vol % to 40 vol %. The alumina containing mixture may be a shear thinning slurry having a viscosity of 1 s−1 at a shear rate of not greater than 900 cP 1, and at viscosity of at least 70 cP at a shear rate of 500 s−1.
In another embodiment, the mixture can comprise at least 30 vol % alumina and the forming of the three dimensional body may be conducted at an applied UV power of at least 3 mW/cm2 and not greater than 12 mW/cm2.
In a further particular embodiment, the alumina particles can be present the mixture in an amount of 16 vol % to 25 vol %, and the forming of the three dimensional body may be conducted at an applied UV power of at least 1.0 mW/cm2 and not greater than 12 mW/cm2.
In another particular embodiment, the mixture can comprise silica particles having an average particle size from 100 nm to 5000 nm and in an amount of 15 to 40 vol %. In a certain aspect, the silica particles can have an average particle size from 1000 nm to 3000 nm and may be present in an amount of 25 vol % to 35 vol %, wherein the mixture is a shear thinning slurry having a viscosity of not greater than 200 cP at a shear rate of 1 s−1 and a viscosity of at least 50 cP at a shear rate of 500 s−.
In a further particular aspect, the method of the present disclosure may employ a mixture comprising at least 25 vol % silica, and the forming of the three dimensional body can be conducted at an applied UV power of at least 1.0 mW/cm2 and not greater than 12 mW/cm2.
According to an embodiment, the mixture may be essentially free of a dye. In this embodiment, the mixture may be formed with solid particles having the proper combination of concentration, average particle size, and coating on the solid particles. A mixture being essentially free of a dye relates to a dye concentration of less than 0.001 vol %. In contrast, radiation curable mixtures which do not contain solid particles and are fully polymer-based, generally require a dye in order to control unwanted photopolymerization.
The total volume of the three-dimensional body created by the process of the present disclosure can be at least 0.1 mm3, such as at least 0.3 mm3, at least 0.5 mm3 or at least 1 mm3. If the process of the present disclosure employs a replenishable reservoir, as shown in
The method of the present disclosure can be further characterized by producing three-dimensional bodies from mixtures having a high content of solid particles, whereby the formed bodies can have an exceptional uniform structure, high strength and high smoothness.
In one embodiment, the method of the present disclosure is characterized that a three-dimensional body including ceramic particles can be continuously manufactured at a high production speed. In one aspect, the creating of the three dimensional body can be completed at a speed rate of at least 25 mm/hr, such as at least 30 mm/hr, at least 40 mm/hr, at least 50 mm/hr, or at least 70 mm/hr.
In a particular embodiment, the three dimensional body of the present disclosure can be subjected to high temperature sintering to remove the radiation curable material and to form a sintered body. If the solid particles of three dimensional body subjected to high temperature sintering are ceramic particles, the sintered body is called hereafter a ceramic body.
The sintering temperature can be at least 900° C., such as at least 950° C., at least 1000° C., at least 1050° C., at least 1100° C., or at least 1150° C. In other aspects, the sintering temperature can be not greater than 1600° C., such as not greater than 1550° C., not greater than 1500° C., or not greater than 1400° C. It will be appreciated that the sintering temperature can be a value between any of the minimum and maximum values noted above, such as from 900° C. to 1600° C., from 1000° C. to 1500° C., or from 1100° C. to 1350° C.
In a certain embodiment, the high temperature sintering can lead to a ceramic body having a density of at least 90% of its theoretical density.
In particular embodiments, the ceramic body can consist essentially of ceramic particles. In one aspect the ceramic body may consist essentially of alumina. In another aspect, the ceramic body can consist essentially of silica. Consisting essentially of ceramic particles means that the ceramic body comprises at least 99 wt % ceramic particles based on the total weight of the ceramic body.
Many different aspects and embodiments are possible. Some of those aspects and embodiments are described herein. After reading this specification, skilled artisans will appreciate that those aspects and embodiments are only illustrative and do not limit the scope of the present invention. Embodiments may be in accordance with any one or more of the embodiments as listed below.
A method of forming a body comprising:
forming a three-dimensional body from a mixture, the mixture comprising at least 15 vol % of solid particles for a total volume of the mixture and a radiation-curable material, wherein forming includes continuous translation and growth of the body from an interface of the mixture.
A method of forming a body comprising:
providing an assembly including a chamber containing a mixture and a construction;
forming a three-dimensional body by continuously creating and attaching a radiation cured translating portion to a carrier plate of the construction and increasing a distance between the carrier plate and the mixture in a continuous manner to create a three-dimensional body within the mixture, wherein during forming the three-dimensional body is adjacent to an interface of an inhibition zone of the mixture,
wherein the mixture comprises a liquid characteristic selected from the group of:
a shear-thinning slurry;
a shear-thinning slurry with a radiation-curable material;
a content of solid particles of at least 15 vol % for a total volume of the mixture;
a yield point of less than 10 Pa;
a viscosity of at least 50 cP at a shear rate of less than about 5 Hz, and a viscosity of less than 1000 cP at a shear rate greater than about 25 Hz;
or a combination thereof.
The method of embodiments 1 or 2, wherein the radiation-curable material comprises a photoinitiator and a polymerizable monomer.
The method of any of embodiments 1 to 3, wherein during forming portions of the mixture are subjected to electromagnetic radiation having a wavelength in a range from 200 nm to 760 nm.
The method of embodiment 4, wherein the electromagnetic radiation has a wavelength within a range from at least 370 nm to not greater than 450 nm.
The method of embodiments 4 or 5, wherein the electromagnetic radiation has an energy within a range from at least 20 mJ/cm2 to not greater than 450 mJ/cm2.
The method of embodiment 6, wherein the electromagnetic radiation has an energy within a range from at least 20 mJ/cm2 to not greater than 200 mJ/cm2.
The method of embodiment 7, wherein the electromagnetic radiation has an energy within a range from 20 mJ/cm2 to 100 mJ/cm2.
The method of embodiment 3, wherein the photoinitiator comprises a free-radical photoinitiator.
The method of embodiment 3, wherein the polymerizable monomer comprises a material selected from the group of acrylates, acrylamides, urethanes, dienes, or a combination thereof.
The method of any of the previous embodiments, wherein the solid particles include ceramic particles, metallic particles, polymeric particles, or any combination thereof.
The method of embodiment 11, wherein the ceramic particles comprise at least one material selected from the group of an oxide, a carbide, a boride, a nitride, a silicide or a combination thereof.
The method of embodiment 12, wherein the ceramic particles comprise at least one material selected from the group of alumina, ceria, zirconia, silica, magnesium-magnesia aluminate (MMA), magnesia, silicon carbide, hydroxyapatite, cordierite, or a combination thereof.
The method of any of embodiment 13, wherein the mixture comprises solid particles selected from the group of alumina, silica, MMA, or zirconia.
The method of any of the previous embodiments, wherein at least a portion of the solid particles include a coating overlying an exterior surface.
The method of embodiment 15, wherein the coated solid particles provide a 50% lower scattering of an applied electromagnetic radiation than corresponding uncoated particles.
The method of embodiment 16, wherein the coated solid particles provide a 90% lower scattering of an applied electromagnetic radiation than the corresponding uncoated particles.
The method of embodiment 15, wherein the coated solid particles provide a 50% lower absorbance of an applied electromagnetic radiation than corresponding uncoated particles.
The method of embodiment 18, wherein the coated solid particles provide a 90% lower absorbance of an applied electromagnetic radiation than the corresponding uncoated particles.
The method of any of the previous embodiments, wherein the solid particles have an average particle size of at least 0.1 μm and not greater than 20 μm.
The method of any of the previous embodiments, wherein the solid particles have a multimodal particle size distribution.
The method of any of the previous embodiments, wherein the solid particles have a particle size distribution comprising a value of function (d50−d10)/d50 of less than 0.8.
The method of any of the previous embodiments, wherein the solid particles have a particle size distribution comprising a value of function (d90−d50)/d50 of less than 1.0.
The method of embodiments 1 or 2, wherein the mixture comprises an inhibition zone wherein the radiation curable material does not cure if subjected to electromagnetic radiation.
The method of embodiment 24, wherein the inhibition zone has a thickness of at least 0.5 μm and not greater than 600 μm.
The method of embodiments 24 or 25, wherein forming comprises selecting solid particles having an average particle size relative to a thickness of the inhibition zone.
The method of embodiments 24 or 25, wherein forming comprises selecting a concentration of the solid particles in the mixture relative to a thickness dimension of the inhibition zone.
The method of embodiment 26, wherein the average particle size of the solid particles is not greater than 25% of the thickness of the inhibition zone.
The method of embodiment 28, wherein the average particle size of the solid particles is not greater than 10% of the thickness of the inhibition zone.
The method of embodiment 2, wherein the chamber further comprises an oxygen-permeable layer.
The method of embodiments 1 or 2, wherein the mixture is essentially free of a dye.
The method of any of embodiments 4 to 31, wherein the applied electromagnetic radiation has a power of at least 0.1 mW/cm2, such as at least 0.5 mW/cm2, at least 1.0 mW/cm2, at least 2 mW/cm2, or at least 3 mW/cm2.
The method of any of embodiments 4 to 32, wherein the applied electromagnetic radiation has a power not greater than 250 mW/cm2, such as not greater than 100 mW/cm2, not greater than 50 mW/cm2, or not greater than 10 mW/cm2.
The method of any of the precedent embodiments, wherein the mixture is a shear thinning slurry.
The method of embodiment 34, wherein the shear thinning slurry is characterized that a decrease in viscosity of the mixture from a shear rate of 0.1 s−1 to a shear rate of 500 s−1 is at least 10 cP, such as at least 30 cP, at least 50 cP, or at least 80 cP.
The method of embodiment 34, wherein shear thinning slurry is characterized that a decrease in viscosity of the mixture from a shear rate of 0.1 s−1 to a shear rate of 500 s−1 is not greater than 1500 cP, such as not greater than 1200 cP, not greater than 1000 cP, or not greater than 800 cP.
The method of any of the precedent embodiments, wherein the mixture comprises alumina particles having an average particle size from 100 nm to 5000 nm in an amount of 15 vol % to 50 vol %.
The method of embodiment 37, wherein the alumina particles have an average particle size from 300 nm to 3000 nm and are present in an amount of 18 vol % to 40 vol %, and wherein the mixture is a shear thinning slurry having a viscosity of not greater than 900 cP at a shear rate of 1 s−1, and at viscosity of at least 70 cP at a shear rate of 500 s−1.
The method of embodiments 37 or 38, wherein the mixture has a viscosity not greater than 150 cP at a shear rate of 500 s−1.
The method of any of embodiments 37 to 39, wherein the mixture comprises at least 30 vol % alumina and the forming of the three dimensional body is conducted at an applied UV power of at least 3 mW/cm2 and not greater than 12 mW/cm2.
The method of any of embodiment 37 to 39, wherein the alumina particles are present in an amount of 16 vol % to 25 vol %, and the forming of the three dimensional body is conducted at an applied UV power of at least 1.0 mW/cm2 and not greater than 12 mW/cm2.
The method of any of embodiments 1 to 36, wherein the mixture comprises silica particles having an average particle size from 100 nm to 5000 nm and in an amount of 15 to 40 vol %.
The method of embodiment 42, wherein the silica particles have an average particle size from 1000 nm to 3000 nm and are present in an amount of 25 vol % to 35 vol %, and wherein the mixture is a shear thinning mixture having a viscosity of not greater than 200 cP at a shear rate of 1 s−1 and a viscosity of at least 50 cP at a shear rate of 500 s−1.
The method of embodiments 42 or 43, wherein the mixture has a viscosity not greater than 100 cP at a shear rate of 500 s−1.
The method of any of embodiments 42 to 44, wherein the mixture comprises at least 25 vol % silica and the forming of the three dimensional body is conducted at an applied UV power of at least 1.0 mW/cm2 and not greater than 12 mW/cm2.
The method of any of the precedent embodiments, further comprising subjecting the three dimensional body to high temperature sintering at a temperature of at least 1000° C.
The method of embodiment 46, wherein high temperature sintering forms a ceramic body, the ceramic body having a density of at least 90% of its theoretical density.
The method of embodiment 47, wherein the ceramic body consists essentially of alumina.
The method of embodiment 47, wherein the ceramic body consists essentially of silica.
The method of any of the precedent embodiments, wherein forming is conducted at a forming speed of at least 25 mm/hr.
The method of any of the precedent embodiments, wherein forming is conducted at a forming speed of at least 60 mm/hr.
A method of forming a body comprising: forming a three-dimensional body using an additive manufacturing process, the three-dimensional body having a content of ceramic solid particles of at least 15 vol % for a total volume of the body, wherein the three-dimensional body has a total volume of at least 0.1 mm3, and wherein forming is completed at a forming speed of at least 25 mm/hr.
The method of embodiment 52, wherein the forming speed is at least 60 mm/hr.
The following non-limiting examples illustrate the present invention.
Example 1 demonstrates the change in cure depth of UV-radiation curable mixtures with different types of ceramic particles. The ceramic particle powders used in the experiments were alumina, zirconia, silica, magnesium-magnesia aluminate (MMA), silicon nitride, silicon carbide, and graphite.
Ceramic slurries were prepared for each type of ceramic powder using as radiation curable material for all samples 1,6 hexanediol diacrylate (Sartomer SR238, hereinafter used as “monomer”) and a photoinitiator (Irgacure 819). A summary of the ceramic powder slurries used in the experiments can be seen in Table 1.
All mixtures E2 to E7 contained a dispersant which insured that the ceramic particles did not settle over a time period of at least 1 hour. Table 2 gives a summary of the settling tests performed to select the appropriate dispersant. Three dispersants (Disperbyk-111, Disperbyk-180, Disperbyk-168) were selected on the basis of their potential chemical affinity to the radiation curable monomer. Mixtures of monomer, specific dispersant and powder were prepared and mixed using a resodyn acoustic mixer and were observed thereafter for settling behavior over the period of four days. The efficiency of each dispersant was assessed by visual inspection. Disperbyk-111 was observed to be the most effective dispersant for the alumina slurries, whereas Dysperbyk-168 was the best dispersant for all the other mixtures.
For the measurement of the cure depth, a chamber was filled with the mixture to be tested (E1 to E7), and the mixture was exposed to a static image made of a series of light dots, wherein the dots differed in their light intensity. The image was projected from a Digital Light Projector connected to a UV lamp (405 nm). The light intensity of each dot was controlled by scaling down the [R G B] intensity of the dots directly on the image. For most curing experiments, the power of the lamp was 30 mW/cm2, and the resin was exposed to the radiation for 60 seconds at a maximum UV exposure of 1800 mJ/cm2 for the dot with the highest light intensity. The thickness of each printed dot was then measured with a micro-caliper to obtain a relationship of cure depth in dependency to the UV exposure.
As can be seen in Table 3 and
It can be further seen from
Table 4 shows the curing sensitivity Dp values obtained from the slopes of
‡Ceramic particles
Radiation curable mixtures with and without Al2O3 (E4 and E1), have been further compared by measuring the thickness of the inhibition zone for each sample with increasing UV exposure.
As can be seen in Table 5 and
It could further be observed that the amount of ceramic particles and the applied UV exposure needed to be carefully balanced in order to create an inhibition zone which can prevent adsorption of cured mixture on the bottom surface of the chamber. At a UV-exposure at 260 mJ/cm2 or higher, the alumina containing slurries did not establish a functioning inhibition zone, and the radiation cured mixture was sticking to the bottom surface of the micro-chamber.
Two different types of oxygen permeable membranes—AF-2400X and PMP—were compared regarding their influence on the thickness of a formed inhibition zone under otherwise equal conditions. AF-2400X is an oxygen permeable Teflon membrane made by Biogeneral, and PMP is a polymethylpentene based membrane, also called TPX, made by MITSUI Chemicals. Both membranes had a thickness of 2.2 mils.
For the experiments, the radiation curable material of Example 1 (CLEAR from Formlabs) was used without the inclusion of Al2O3. As can be seen in Table 6, in the presence of the AF-2400X membrane, the formed inhibition zone is much larger than the inhibition zone created when using a PMP membrane. This indicates that AF-2400X allows the penetration of higher amounts of oxygen in comparison to PMP membrane.
Continuous forming of a three-dimensional body comprising Al2O3
A mixture was prepared containing 20 vol % Al2O3 (Almatis A16) (equals 48.1 wt % Al2O3), 27.8 wt % radiation curable monomer (Sartomer SR 238), 20.6 wt % radiation curable oligomer (Formlab resin clear), 0.22 wt % of a photo initiator (Irgacure 819), and 3.2 wt % dispersant (Disperbyk-111).
The mixture was placed in a chamber of an assembly having a similar design as shown in
A carrier plate attached to a vertically movable construction was placed into the mixture of the chamber at a distance of about 10 μm above the surface of the transparent window. The mixture was radiated with the UV LEDs, and with a minor time delay of about 1 to 2 seconds, the carrier plate was started to continuously move upwards, pulling a rod-shaped body out of the mixture. The experiment was repeatedly conducted at different continuous forming speeds, such as 30 mm/hour, 60 mm/hour, and 90 mm/hour, as well as at different UV exposures (see Table 7).
A picture of the rod-shaped body formed at a speed of 1.5 mm/min and a UV power of 0.56 mW/cm2 is shown in
A mixture was prepared with the same components as in Example 4, but by increasing the amount of Al2O3 to 35 vol % (corresponding to 66.1 wt %). The exact formulation was as follows: 66.61 wt % Al2O3 (A16 Almatis), 17.52 wt % radiation curable monomer (Sartomer SR 238), 13.07 wt % radiation curable oligomer (Formlab resin clear), 0.29 wt % of a photo initiator (Irgacure 819), and 2.52 wt % dispersant (Disperbyk-111). The mixture was not printable because of a too high viscosity. One reason for the high viscosity was the high initial viscosity of the radiation curable oligomer (Formlab resin clear). Based thereon, for the further experiments with mixtures of high solid content (above 25 vol %), no oligomer component was included into the compositions.
Continuous forming of three-dimensional body comprising Al2O3 at different light intensities.
A mixture containing 35 vol % Al2O3 (Almatis A16) was prepared according to the composition as shown in Table 1, mixture E2.
A three dimensional body was formed according to the same method and system as described in Example 4. The body was formed at a speed of 60 mm/hour, but at two different applied UV intensities: 1.76 mW/cm2 and 7.06 mW/cm2. As can be seen in
Continuous forming of three-dimensional body comprising silica at different light intensities.
A mixture containing 30 vol % silica was prepared according to the composition shown in Table 1, mixture E4.
A three dimensional body was formed according to the same method and system as described in Example 4. The body was formed at a speed of 60 mm/hour, and at two different applied UV intensities: 1.76 mW/cm2 and 7.06 mW/cm2. Cylinders of high quality at both UV powers could be formed (see
Continuous forming of three-dimensional body comprising MMA at different light intensities
A mixture containing 28 vol % MMA was prepared according to the composition shown in Table 1, mixture E5.
A three dimensional body was formed according to the same method and system as described in Example 4. The body was formed at a speed of 60 mm/hour, and at two different applied UV intensities: 3.53 mW/cm2 and 7.06 mW/cm2. As can be seen in
Continuous forming of three-dimensional body comprising zirconia with varying light intensity
A mixture containing 27.6 vol % zirconia was prepared according to the composition shown in Table 1, mixture E3.
A three dimensional body was formed according to the same method and system as described in Example 4. The body was formed at a speed of 60 mm/hour, and at two different applied UV intensities: 7.06 mW/cm2 and 11.76 mW/cm2. As can be seen in
Table 8: Summary of Examples 4 to 9: Continuous forming of three-dimensional bodies at a forming speed of 60 mm/hour with different types of ceramic particles and different light intensities
Continuous forming of three-dimensional bodies comprising silica with different amounts of silica in mixtures.
Three mixtures were prepared with varying amounts of silica in the mixtures: 30 vol % (E8), 40.3 vol % (E9) and 45.2 vol % (E10). The average silica particle size in all three mixtures was 1.7 μm. All mixtures further contained monomer (Sartomer SR238), photoinitiator (Irgacure 819), and dispersant Dysperbyk-168).
Similar as in Example 1, the cure depths of the mixtures E8, E9, and E10 were measured with increasing UV exposure and the curing sensitivity Dp for each mixture were calculated from the slope of the linear curves (see
As another characterization of mixtures E8, E9, and E10, the viscosities with varying shear rate were measured for of each mixture.
All viscosity measurements of the mixtures of the present disclosure under certain shear rates were conducted with a Discovery HR-1 Rotational Rheometer using a cone and plate geometry with a 40 mm diameter and a 2 degree cone angle, wherein the shear rate was constant across the entire sample. The tests were done in flow mode at a temperature of 25° C.
As can be seen in
Three dimensional bodies were formed from mixtures E8, E9, and E10 according to the same method and system as described in Example 4. The bodies were formed at a speed of 60 mm/hour, and at a UV intensity of 7.06 mW/cm2. As can be seen in
Not to be bound to theory, the quality differences between the formed bodies of mixtures E8, E9, and E10 indicate that advantageous for the forming of a high quality body is a shear thinning behavior of the mixtures.
Continuous forming of three-dimensional bodies comprising alumina with different average particle size.
Three mixtures were prepared containing alumina particles in an amount of 35 vol % but with varying average particle size, i.e., 500 nm (mixture E11), 2 μm (mixture E12), and 10 μm (mixture E13). All mixtures further contained monomer (Sartomer SR238), photoinitiator (Irgacure 819), and dispersant Dysperbyk-111).
For evaluating printability of the mixtures, the cure depth in dependency to the UV exposure (405 nm) was measured and the sensitivity Dp calculated from the slopes of the curves, as described in Example 1. As can be seen in
Although mixture E13 had the highest sensitivity, its viscosity behavior made it unsuitable for printing a body. The viscosity measurement are shown in
As a result, continuous printing was not possible for mixture E13. In comparison, both mixtures E11 and E12 were suitable for printing, and cylindrical bodies with good quality were printed at a forming speed of 60 mm/hour and a UV intensity of 7.06 mW/cm2. A summary of the results of Example 11 can be seen in Table 10.
Forming a complex flower shape with alumina comprising slurry followed by de-binding and sintering
A three dimensional flower-shaped green body was formed using the same mixture and method as described in Example 2 (alumina comprising mixture, E2) The flower-shaped body was formed at a speed of 60 mm/hour, and an applied UV intensity of 6 mW/cm2 (see
After the forming of the green body, the following de-binding and sintering regime was applied:
Heating at a rate of 1° C./min up to 325° C.; holding the temperature for 30 minutes at 325° C., heating at rate of 1° C./min up to 650° C.; holding the temperature for 1 hour at 650° C.; heating at a rate of 5° C./min up to 1480° C.; holding the temperature for 30 minutes at 1480° C.; heating at a rate of 1° C./min up to 1550° C.; holding the temperature for 1 hour at 1550° C.; cooling down at a rate of 5° C./min to room temperature.
After the high temperature sintering, the flower-shaped body have kept its integrity, despite a shrinkage of about 23%.
The microstructure of the sintered ceramic flower was investigated using Scanning Electron Microscope (SEM) technology. Apart of a few minor surface delaminations, no larger cracks or defects could be observed. Cross-sections of individual posts of the flower were polished and thermally etched at 50° C. below the maximal sintering temperature for 30 minutes. As can be seen in
The high density of the sintered ceramic flower was also confirmed by Archimedes and Helium picnometry methods. The average density was 92.7% of the theoretical density of alumina if measured by the Archimedes method, and 93% of the theoretical density was measured with the Helium pycnometry method.
In the foregoing specification, the concepts have been described with reference to specific embodiments. However, one of ordinary skill in the art appreciates that various modifications and changes can be made without departing from the scope of the invention as set forth in the claims below. Accordingly, the specification and figures are to be regarded in an illustrative rather than a restrictive sense, and all such modifications are intended to be included within the scope of the invention.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/US2016/057061 | 10/14/2016 | WO | 00 |
| Number | Date | Country | |
|---|---|---|---|
| 62242150 | Oct 2015 | US |
