LITHOGRAPHY-BASED PROCESS FOR THE PRODUCTION OF TRANSPARENT CERAMIC BODIES WITH AT LEAST TWO ZONES OF DIFFERENT COMPOSITION AND TRANSPARENT CERAMIC BODIES THUS OBTAINED
20230138537 · 2023-05-04
Inventors
- Valentina BIASINI (CESENA, IT)
- Jan HOSTASA (FAENZA, IT)
- Laura ESPOSITO (FAENZA, IT)
- Andreana PIANCASTELLI (FAENZA, IT)
- Guido TOCI (FIRENZE, IT)
- Martin SCHWENTENWEIN (ZEMENDORF, AT)
- Dominik Philipp BROUCZEK (SCHWECHAT, AT)
Cpc classification
C04B2235/3222
CHEMISTRY; METALLURGY
B33Y10/00
PERFORMING OPERATIONS; TRANSPORTING
B33Y70/00
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/3286
CHEMISTRY; METALLURGY
C04B2235/549
CHEMISTRY; METALLURGY
B28B11/243
PERFORMING OPERATIONS; TRANSPORTING
B33Y40/20
PERFORMING OPERATIONS; TRANSPORTING
B62J17/00
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/3208
CHEMISTRY; METALLURGY
C04B35/2675
CHEMISTRY; METALLURGY
C04B2235/3206
CHEMISTRY; METALLURGY
C04B2237/704
CHEMISTRY; METALLURGY
C04B2235/5436
CHEMISTRY; METALLURGY
C04B2235/3225
CHEMISTRY; METALLURGY
B32B18/00
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/3418
CHEMISTRY; METALLURGY
C04B2235/72
CHEMISTRY; METALLURGY
C04B2235/6026
CHEMISTRY; METALLURGY
C04B2235/9653
CHEMISTRY; METALLURGY
C04B2235/3229
CHEMISTRY; METALLURGY
B28B1/001
PERFORMING OPERATIONS; TRANSPORTING
C04B2235/5445
CHEMISTRY; METALLURGY
C04B2235/6581
CHEMISTRY; METALLURGY
C04B2235/3224
CHEMISTRY; METALLURGY
International classification
C04B35/626
CHEMISTRY; METALLURGY
B28B1/00
PERFORMING OPERATIONS; TRANSPORTING
B28B11/24
PERFORMING OPERATIONS; TRANSPORTING
B33Y10/00
PERFORMING OPERATIONS; TRANSPORTING
B33Y40/20
PERFORMING OPERATIONS; TRANSPORTING
Abstract
It is described a process for producing transparent ceramic bodies with at least two zones having different garnet composition, in particular in which one of said zones has composition Y.sub.3AI.sub.5O.sub.12. The invention is especially useful for the production of transparent ceramic bodies having preset complex shapes and/or a controlled complex distribution of doping ions.
Claims
1. A process for the production of a transparent ceramic body, comprising the steps of: a) preparing a first suspension comprising: 1) a solvent; 2) a mixture of powders of oxides, hydroxides, nitrates or chlorides of metals in the stoichiometric ratio required to produce an oxide phase A.sub.3B.sub.5O.sub.12+x, wherein is −0.1≤x≤0.1, A is selected among Y, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu and mixtures thereof, and B is selected among Al, Fe, Cr, Sc, Ga and mixtures thereof; 3) a sintering aid selected among silicon oxide in the form of powder, a tetraalkylorthosilicate, calcium oxide powder, a calcium oxide precursor, magnesium oxide powder, a magnesium oxide precursor, or a mixture thereof; 4) a dispersant selected among polyethylene glycol, menhaden fish oil, phosphate esters, dicarboxylic acids, stearic acid and silanes; b) extracting the solvent from the suspension of step a) obtaining a mixture; c) preparing a homogeneous slurry comprising the mixture of step b) and a photocurable resin; d) preparing at least a second suspension comprising: 1′) a solvent; 2′) a mixture of powders of oxides, hydroxides, nitrates or chlorides of metals in the stoichiometric ratio required to produce an oxide phase A.sub.3B.sub.5O.sub.12+x, wherein is −0.1≤x≤0.1, A is selected among Y, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu and mixtures thereof, and B is selected among Al, Fe, Cr, Sc, Ga and mixtures thereof; 3′) a sintering aid selected among silicon oxide in the form of powder, a tetraalkylorthosilicate, calcium oxide powder, a calcium oxide precursor, magnesium oxide powder, a magnesium oxide precursor, or a mixture thereof; 4′) a dispersant selected among polyethylene glycol, menhaden fish oil, phosphate esters, dicarboxylic acids, stearic acid and silanes; e) extracting the solvent from the suspension of step d) obtaining a mixture; f) preparing a homogeneous slurry comprising the mixture of step e) and a photocurable resin; g) operating at a temperature between 20 and 30° C., forming a deposit comprising layers of the slurries of steps c) and f) by a layer-by-layer 3D printing technique wherein, after the deposition of each layer of slurry, a photopolymerization operation of the photocurable resin is carried out, and a cleansing operation of a series of photopolymerized layers of a first composition is carried out before depositing on it or next to it a layer of slurry of a second composition to remove the non-polymerized slurry of first composition, obtaining a consolidated body; h) subjecting the consolidated body of step g) to a thermal treatment in air or in an oxygen-rich atmosphere at a temperature in the range 100 to 1000° C. for removing the organic and volatile components of the consolidated body, obtaining a degreased body; i) subjecting the degreased body of step h) to a sintering thermal treatment in vacuum at a temperature in the range from 1600° C. to 1900° C. for a time in the range from 6 h to 32 h obtaining a sintered body; or i′) subjecting the degreased body of step h) to a sintering thermal treatment in vacuum at a temperature in the range from 1400° C. to 1800° C. for a time in the range from 2 h to 20 h followed by hot isostatic pressing with an applied pressure in the range from 100 to 300 bar at a temperature in the range from 1400° C. to 1800° C. for a time in the range from 1 h to 4 h obtaining a sintered body; in which said first suspension and said at least one second suspension have different compositions.
2. The process according to claim 1, further comprising a step j) in which the sintered body obtained in step i) or in step i′) is subjected to an annealing treatment in an oxidizing or a reducing atmosphere, in order to adjust the oxidation state of possible dopants.
3. The process according to claim 1, wherein the powders of metal oxides, hydroxides, nitrates or chlorides of mixtures 2) and 2′) have a mean grain size lower than 10 μm and preferably lower than 5 μm, an aspect ratio between 0.8 and 1.0 and a purity of at least 99% and preferably higher than 99.99%.
4. The process according to claim 1 wherein, when the sintering aids 3 and 3′) are or comprise compounds in form of powders, these have a grain size lower than 2 μm, and preferably lower than 1 μm.
5. The process according to claim 1 wherein the solvent, 1) or 1′), is an alcohol, and its weight is between 1.5 and 2.5 times the weight of 2) or 2′), the mixture of powders.
6. The process according to claim 1 wherein sintering aids 3) and 3′) are employed in a weight between 0.0005 and 0.003 g per gram respectively of the mixtures 2) and 2′) of powders of metal oxides, hydroxides, nitrates or chlorides.
7. The process according to claim 1 wherein the photocurable resin is employed in an amount between 50 and 60% in volume of the slurry of step c) or f).
8. The process according to claim 1 wherein the amount of dispersant 4) is between 1.5 and 2.5% by weight of the suspension prepared in step a) and the amount of dispersant 4′) is between 1.5 and 2.5% by weight of the suspension prepared in step d).
9. The process according to claim 1 wherein, wherein step g) is carried out by lithography-based ceramic manufacturing (LCM).
10. The process according to claim 1 wherein step h) is carried out at a temperature in the range 550-800° C. for a time up to 72 hours with a heating rate between 0.05° C./min and 2° C./min, and below 0.25° C./min in the range of temperatures between 115 and 250° C.
11. A transparent ceramic body with a non-uniform and controlled spatial distribution of the chemical composition obtained according to claim 1, in which different zones have different compositions of general formula A.sub.3B.sub.5O.sub.12+x, wherein is −0.1≤x≤0.1, A is selected among Y, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er, Tm, Yb, Lu, and mixtures thereof, and B is selected among Al, Fe, Cr, Sc, Ga and mixtures thereof.
12. The transparent ceramic body according to claim 11, in which at least one of said zones has composition Y.sub.3Al.sub.5O.sub.12 or a composition obtained by partial substitution of Y and/or Al in the composition Y.sub.3Al.sub.5O.sub.12.
13. The transparent ceramic body according to claim 11, consisting of two layers of different composition.
14. The transparent ceramic body according to claim 11, consisting of a single part with a graded profile of composition.
15. The transparent ceramic body according to claim 11 consisting of concentric zones, in which outer zones have different, uniform composition, and a central zone has a graded profile of composition across its thickness.
16. The transparent ceramic body according to claim 11 consisting of concentric zones of different composition, in which an outer zone has a radially graded profile of composition, and the central zone has a hemispherically graded profile of composition.
Description
BRIEF DESCRIPTION OF THE FIGURES
[0054]
[0055]
[0056]
DETAILED DESCRIPTION OF THE INVENTION
[0057] The inventors have observed that, although methods for the production of transparent ceramic bodies were generally known in the art, also based on 3D printing techniques, only the combination of conditions and steps of the process of the invention allows to obtain a complete control of the composition profile of the final transparent ceramic bodies in the three spatial directions; in particular, the deposition of layers at temperatures between 20 and 30° C., the use of a dispersant and the cleansing of any layer after photopolymerization, are essential to obtain the desired results.
[0058] The invention will be described below with reference to the figures.
[0059] In its first aspect, the invention refers to a process for producing transparent ceramic bodies having preset complex shapes and/or a controlled complex distribution of doping ions.
[0060] For the objects of the invention, the compounds used in the process must be highly pure; for instance, the oxides, hydroxides or nitrates mentioned below must have a purity of at least 99%, and preferably higher than 99.99%.
[0061] For the sake of simplicity, the process is described below with reference to the preparation and use of two different slurries, but it will be apparent to the skilled person that the steps of the process can be carried out also with three or more slurries, to obtain transparent ceramic bodies of more complex composition profiles.
[0062] The process comprises steps a) to i) or i′), or steps a) to j), as described in detail below.
[0063] The first step of the process, step a), consists in preparing a homogeneous slurry of: 1) a solvent, 2) a mixture of powders of precursors of the desired garnet phase, 3) one or more sintering aids, and 4) a dispersant.
[0064] The solvent, 1), may be selected among alcohols, e.g., ethanol or isopropanol, and usually the weight of the solvent is between 1.5 and 2.5 times, preferably about twice, the weight of 2), the mixture of powders.
[0065] Component 2) consists in mixed powders of oxides, hydroxides, nitrates or chlorides of metals, in the exact stoichiometric ratio required to produce the desired oxide phase A.sub.3B.sub.5O.sub.12+x, wherein A, B and x have the meanings indicated above. These powders must have a mean grain size lower than 10 μm, and preferably lower than 5 μm; besides, the shape of the powder grains must be essentially or nearly spherical, with an aspect ratio between 0.8 and 1.0.
[0066] These powders are of common commercial availability from many suppliers; as an example, rare earth oxides are sold by Alfa Aesar (USA) and Merck (Germany).
[0067] The more common oxidation state of rare earth elements is +3, but also oxidation states +2 (e.g., Sm.sup.2+, Eu.sup.2+ or Yb.sup.2+) or +4 (e.g., Ce.sup.4+) are possible; similarly, the metals Sc, Fe and Cr may exist in oxidation state +3 but also in other oxidations states. The parameter x, which may vary between −0.1 and 0.1, accounts for the variability of stoichiometry of oxygen due to the presence in the material of ions with oxidation state different from +3; x is positive if, on average, the oxidation state of the ions of metals A and B is >3, and it is negative if on average the oxidation state of said metals is <3. Given the formula of the desired specific composition, the calculation of amounts of the different oxides, hydroxides or nitrates or chlorides to be used for the preparation of the mixture of step a) is straightforward for the average chemist.
[0068] The sintering aid, 3), is selected among silicon oxide (SiO.sub.2, commonly referred to as silica) powder, a tetraalkylorthosilicate (general formula Si(OR).sub.4, where R is generally a C.sub.1-C.sub.4 alkyl), calcium oxide powder, a calcium oxide precursor, magnesium oxide powder, a magnesium oxide precursor, or a mixture thereof. This component makes easier and more efficient the sintering in step i) or i′). When the component used as sintering aid is, or comprises compounds, in the form of powders, these must have a grain size lower than 2 μm, and preferably lower than 1 μm. A useful form of silicon oxide is colloidal silica, a suspension of silica powder consisting of aggregates of silica particles of nanometric size. The sintering aid component, when used as oxide, is added in a weight between 0.0005 and 0.003 g per gram of the mixture 2) of precursors of the garnet phase.
[0069] Finally, the dispersant, 4), is selected among polyethylene glycol, menhaden fish oil, phosphate esters, dicarboxylic acids, stearic acid and silanes. Polyethylene glycol is commonly referred to as PEG; menhaden fish oil, in the following also indicated by the abbreviation MFO, is preferably used blown (that is, treated by blowing air in it to cause a partial oxidation of its unsaturated bonds).
[0070] All these substances are commercially available. The molecular weight of PEG useful for the aims of the invention is between 200 and 600 Da. The amount of dispersant is between 0.5 and 5%, preferably between 1.5 and 2.5% by weight, of the suspension of step a).
[0071] Components 1), 2), 3) and 4) may be homogenized with any mixing method, obtaining a homogeneous suspension.
[0072] Step b) of the process of the invention consists in the extraction of the solvent from the suspension prepared in step a), performed by any method, obtaining a wet mixture.
[0073] Step c) of the process of the invention consists of preparing of homogeneous slurry of the mixture obtained in step b) and a photocurable resin.
[0074] Photocurable resins are widely known and extremely common in particular in the field of production of semiconductors and microelectromechanical systems (MEMS), and are sold by many suppliers; a suitable photocurable resin useful for the objects of the invention is for example a mixture of 1,6-hexanediol diacrylate, an acrylated oligoamine, benzyl alcohol, camphorquinone and ethyl 4-(dimethylamino)benzoate. The slurry may be homogenized with any mixing method. The total amount of the photocurable resin is between 50 and 60% by volume of the slurry.
[0075] Steps d) to f) of the process of the invention consists of preparation of a second homogeneous slurry. The components of this slurry, as well as their weight or volume ratios, are the same as in the slurry prepared in steps a) to c), but the specific compositions of the first and second slurries employed in the production of a ceramic body must be different. The total amount of the photocurable resin in the two slurries must not differ by more than 3% by volume so that the difference in linear shrinkage between the parts printed with them is lower than 3%.
[0076] In case more than two slurry are prepared and used, these last conditions must be observed for all slurries, that is, these will all have different compositions, and the total amount of resin must not differ by more than 3% by volume between any pair of resins used.
[0077] In step g), the slurries prepared in steps c) and f) are used to form a deposit of desired configuration by 3D printing, by depositing layers of the first and second slurries according to a preset temporal order of deposition and pattern, followed by cleansing before any change of slurry. Each step of layer deposition must take place at a temperature in the range between 20 and 30° C.; the inventors have observed that, operating at temperatures higher than 30° C., a selective sedimentation of the oxides takes place in the printed layers, while at temperatures below 20° C. the slurries are difficult to dispense and spread.
[0078] The preferred technique for the aims of the invention is lithography-based ceramic manufacturing (LCM), a variant of stereolithography. In this technique, a thin layer of the first and second slurries prepared in steps c) and f) is deposited on a substrate, which is a sample holder in the first passage, and already consolidated layers in the next passages; each deposited layer has generally a thickness of about 10 to 100 μm, and is deposited according to a preset geometry, defined through CAD design, and consolidated by light irradiation with the use of suitable physical or digital masks.
[0079] The LCM method can be described as follows: a strong LED with a defined light spectrum exposes a mirror array (Digital Mirror Device—DMD). The DMD partially transmits the light (individual mirrors on position 1) or sends the light to an absorption field (individual mirrors on position 0). The forwarded light is projected through a lens as a pixel pattern (exposure field) onto the vat that contains the slurry. This selective exposure of the photosensitive material causes a hardening of the material at the exposed areas by photopolymerisation. In this process, photocurable organic binders, in which ceramic particles are homogeneously dispersed, are applied in layers and then cured area-wise according to the method described above. The photopolymerisation light wavelength depends on the used resin and is generally indicated by the producer; with the preferred resins of the invention, the photopolymerisation wavelength is between 375 and 460 nm.
[0080] The construction of a consolidated body is thus achieved layer-by-layer, in cycles comprising an operation of slurry deposition followed by an operation of photopolymerization of the resin of the layer. Any time the structure of the desired final body requires the deposition, in contact with the already consolidated layers (i.e., over and/or adjacent to said consolidated layers), of a slurry having a different composition from the slurry with which said consolidated layers have been formed, the intermediate product obtained after the last photopolymerization operation must be cleansed, for instance with the use of solvents, to remove non-consolidated remainders of the previous slurry.
[0081] In the consolidated body thus obtained, the particles of the various oxides are embedded in a matrix of hardened polymer obtained by photopolymerization (“photocuring”) of the resin. This consolidated body has already the shape and the desired profile of composition in the three spatial directions of the final transparent ceramic body.
[0082] The next step of the process, h), consists in the removal of the polymer produced by the photocuring of the resin, of the dispersant, and of other possible volatile components of the consolidated body. This operation is called “debinding” and is preferably carried out in air or an oxygen-rich atmosphere. In this step the consolidated body is subjected to a thermal treatment carried out by bringing it from room temperature to a temperature from 100 to 1000° C., preferably in the range 550-800° C., in up to 72 hours; heating in this phase must be not too rapid, to avoid local accumulations of gases generated by decomposition of the polymer or evaporation of light compounds, which could cause deformation of the body or even pressure bursts that could destroy it. In particular, the heating rate must be between 0.05° C./min and 2° C./min, and preferably below 0.25° C./min in the range between 115 and 250° C. The product obtained as a result of this step is a debinded body with a density from 40 to 60% of the full density.
[0083] The following step of the process consists in the sintering in vacuum of the debinded body to obtain the final ceramic body. By “vacuum” it is intended a pressure lower than 10.sup.−1 Pa.
[0084] Sintering may be carried out according to two possible alternative methods, namely, performing a purely thermal sintering step i), or a thermal sintering step followed by hot isostatic pressing according to step i′). During either of these steps, the garnet phases are formed from the oxides of mixtures 2) and 2′) and the material densifies, i.e., the porosity of the debinded body is removed.
[0085] Step i) is carried out by subjecting the debinded body of step h) to a thermal treatment in vacuum at a temperature in the range from 1600° C. to 1900° C. for a time in the range from 6 h to 32 h, obtaining the transparent ceramic body object of the invention.
[0086] Step i′) is carried out by subjecting the debinded body of step h) to a sintering thermal treatment in vacuum at a temperature in the range from 1400° C. to 1800° C. for a time in the range from 2 h to 20 h followed by hot isostatic pressing (HIP) with an applied pressure in the range from 100 to 300 bar at a temperature in the range from 1400° C. to 1800° C. for a time in the range from 1 h to 4 h, obtaining the transparent ceramic body object of the invention. HIP may be performed with the aid of a gas and a compressor and setting the desired sintering temperature. As a rule, higher pressures allow working at lower temperatures; this slows down grain growth, thus providing an advantage in terms of transparency.
[0087] In both steps i) or i′), the heating rate in the temperature range 1200-1600° C. must be below 100° C./h.
[0088] A vacuum furnace with a clean atmosphere (graphite-free) is preferably used for the sintering process in either of steps i) or i′).
[0089] The process may further comprise an optional step j), in which the transparent ceramic body obtained in step i) or i′) is subjected to an annealing treatment in oxidizing or reducing atmosphere, directed to bringing the dopant ions into a desired oxidation state; this may be necessary, for instance, if dopant ions have been oxidized during debinding step h), or reduced during sintering steps i) or i′) which are carried out in vacuum.
[0090] In a second aspect thereof, the invention provides transparent ceramic bodies that may be used as elements of optical systems, in production, amplification, shaping or guiding of laser beams, as scintillators and other similar applications.
[0091] The preferred bodies of the invention are based on two YAG compositions modified with doping ions or on one pure YAG composition and one modified with doping ions.
[0092] The process of the invention is useful and advantageous for the production of transparent ceramic bodies having a non-uniform, controlled spatial distribution of the doping ions in the three spatial directions, both in case of bodies of simple shape and with complex shapes.
[0093] A few examples of possible transparent ceramic bodies that can be produced with the process of the invention are described below.
[0094] For the sake of simplicity, in the Figures described below the transparent ceramic bodies are mostly shown as disc-shaped, but with the process of the invention obviously other shapes can be produced; bodies similar to the one shown in the Figures below (i.e., layered bodies or bodies with graded profiles of dopant concentration, even in complex configurations) could have any shape, e.g. square, rectangular, or other polygonal or even irregular shapes; in the Figures both 2D and 3D structures are represented, as with the process of the invention it is possible to produce also complex 3D shapes and 3D distribution of the dopants.
[0095]
[0096]
[0097]
[0098]
[0099]
[0100] In particular,
[0101]
[0102] The invention is further illustrated by the following examples.
Example 1
[0103] This example refers to the preparation of a sample of Yb-doped YAG having composition Yb.sub.0.3Y.sub.2.7Al.sub.5O.sub.12.
[0104] In the preparation, commercially available raw materials were used, Al.sub.2O.sub.3TM-DAR produced by Taimei Chemicals CO., Ltd, Y.sub.2O.sub.3 REacton® produced by Alfa Aesar and Yb.sub.2O.sub.3 produced by Sigma Aldrich. All powders had a purity level ≥99.9%.
[0105] The oxide powders were weighed according to the stoichiometry of 10% atomic substitution of Y with Yb (Yb.sub.0.3Y.sub.2.7Al.sub.5O.sub.12), i.e., Al.sub.2O.sub.341.19 g, Y.sub.2O.sub.3 49.26 g and Yb.sub.2O.sub.3 9.55 g. The mixture of oxides powders was mixed for 48 hours with 200 g of ethanol and 0.5 g of tetraethyl orthosilicate (Sigma Aldrich) as sintering agent by ball milling in plastic jars using 300 g Al.sub.2O.sub.3 milling media with diameter ranging from 0.5 to 2 cm. The ethanol was then extracted by rotary evaporation. The obtained powders were then mixed with 1,6-hexanediol diacrylate, an acrylated oligoamine (Genomer* 5695, RAHN AG, Switzerland) and benzyl alcohol using a planetary mill at 300 rpm for 30 min. Afterwards, camphorquinone and ethyl 4-(dimethylamino)benzoate were added as photo-initiators and the slurry was ball milled for 24 h, obtaining a photocurable suspension. The solids loading was 42 vol %.
[0106] Printing was done at 25° C., with a layer thickness of 20 μm and an exposure energy of 170 mJ/cm.sup.2. Afterwards the printed body was cleaned and dried at 120° C.
[0107] The size of the printed sample was 13.5 mm×13 mm with a thickness of 1.75 mm. Debinding was performed in air at the temperature of 600° C. Sintering was performed in a vacuum furnace with tungsten heating elements at temperature 1750° C. with soaking time of 16 h. The sintered body was mirror polished and annealed in air until the Yb.sup.2+ ions, that were produced during vacuum sintering, were oxidised to Yb.sup.3+. Finally, the sample was polished with diamond pastes with grain size from 30 μm down to 0.25 μm using standard optical polishing machines.
Example 2
[0108] This example refers to the optical characterization of the sample of doped YAG produced in Example 1.
[0109] The Yb.sub.0.3Y.sub.2.7Al.sub.5O.sub.12 sample of Example 1 was tested in a laser cavity, longitudinally pumped by a fiber coupled semiconductor laser. This is a typical test bed to assess the laser emission performances of candidate laser materials. Laser emission was obtained from the sample, at a wavelength of 1030 nm, with a maximum slope efficiency of 17% and a maximum output power of 2.2 W, with an absorbed pump power of 13.6 W (conversion efficiency 15.5%), under quasi-continuous pumping conditions.
Example 3
[0110] This example refers to the preparation of a sample of YAG/Yb-doped YAG (wherein YAG has composition Y.sub.3Al.sub.5O.sub.12 and the doped YAG has composition Yb.sub.0.3Y.sub.2.7Al.sub.5O.sub.12) with a side-by-side structure, having a geometry as shown in
[0111] In the preparation, commercially available raw materials were used, Al.sub.2O.sub.3TM-DAR produced by Taimei Chemicals CO., Ltd, Y.sub.2O.sub.3 REacton® produced by Alfa Aesar and Yb.sub.2O.sub.3 produced by Sigma Aldrich. All powders had a purity level 99.9%. Two mixtures were prepared.
[0112] For the first mixture, oxide powders were weighed according to the stoichiometry of 10% atomic substitution of Y with Yb (Yb.sub.0.3Y.sub.2.7Al.sub.5O.sub.12), i.e., Al.sub.2O.sub.341.19 g, Y.sub.2O.sub.3 49.26 g and Yb.sub.2O.sub.3 9.55 g. The mixture of oxide powders was mixed for 48 hours with 200 g of ethanol, 0.5 g of tetraethyl orthosilicate (Sigma Aldrich) as sintering agent and 2.0 g of MFO (Blown Menhaden Z3/Defloc Z3, Werner G. Smith, Inc.) by ball milling in plastic jars using 300 g Al.sub.2O.sub.3 milling media with diameter ranging from 0.5 to 2 cm. The ethanol was then extracted by rotary evaporation. The obtained powders were then mixed with 1,6-hexanediol diacrylate, an acrylated oligoamine (Genomer* 5695, RAHN AG, Switzerland) and benzyl alcohol using a planetary mill at 300 rpm for 30 min. Afterwards, camphorquinone and ethyl 4-(dimethylamino)benzoate were added as photo-initiators and the slurry was ball milled for 24 h, obtaining a photocurable suspension. The solids loading was 42 vol %.
[0113] For the second mixture, oxide powders were weighed according to the stoichiometry of YAG (Y.sub.3Al.sub.5O.sub.12), i.e., Al.sub.2O.sub.342.94 g, Y.sub.2O.sub.3 57.06 g. The mixture of oxides powders was mixed for 48 hours with 200 g of ethanol, 0.5 g of tetraethyl orthosilicate (Sigma Aldrich) as sintering agent and 2.0 g of MFO (Blown Menhaden Z3/Defloc Z3, Werner G. Smith, Inc.) by ball milling in plastic jars using 300 g Al.sub.2O.sub.3 milling media with diameter ranging from 0.5 to 2 cm. The ethanol was then extracted by rotary evaporation. The obtained powders were then mixed with 1,6-hexanediol diacrylate, Genomer* 5695 and benzyl alcohol using a planetary mill at 300 rpm for 30 min. Afterwards, camphorquinone and ethyl 4-(dimethylamino)benzoate were added as photo-initiators and the slurry was ball milled for 24 h, obtaining a photocurable suspension. The solids loading was 42 vol %.
[0114] Printing was done at 25° C., with a layer thickness of 20 μm and an exposure energy of 170 mJ/cm.sup.2.
[0115] Half of each 20 μm layer was printed with the first mixture and half with the second mixture. The cleansing operation followed each change of mixture, to completely remove the unpolymerized slurry from the printed body.
[0116] Afterwards the printed body was cleaned and dried at 120° C.
[0117] The size of the printed sample was 13.5 mm×13 mm with a thickness of 1.75 mm. Debinding was performed in air at 600° C. Sintering was performed in a vacuum furnace with tungsten heating elements at temperature 1750° C. with soaking time of 16 h. The sintered body was mirror polished and annealed in air until the Yb.sup.2+ ions, that were produced during vacuum sintering, were oxidised to Yb.sup.3+. Finally, the sample was polished with diamond pastes with grain size from 30 μm down to 0.25 μm using standard optical polishing machines.
[0118] The desired structure was obtained.
Example 4 (Comparative)
[0119] The procedure of Example 3 was repeated identically, with the only difference that the cleansing operation after each change of mixture in the printing phase was not carried out.
[0120] The desired structure was not obtained due to the cross-contamination of slurries that led to a mixed composition in both parts of the body.
Example 5 (Comparative)
[0121] The procedure of Example 3 was repeated identically, with the only difference that the printing step was carried out at 40° C.
[0122] Due to the rheological properties of the slurry at this temperature, the desired side-by-side structure could not be obtained.
Example 6 (Comparative)
[0123] The procedure of Example 3 was repeated identically, with the only difference that the two slurries of precursors of the ceramic phases were prepared using 2.0 g of the commercial dispersant Tego® Dispers 652 (Evonik Industries AG, Essen, Germany) in place of 2.0 g of MFO.
[0124] The desired results were not obtained because the viscosity of the slurries was too high to allow printing.
Example 7
[0125] This example refers to the preparation of the complex, 3D structure showed in
[0126] Two slurries were prepared as described in Example 3.
[0127] Printing was done at 25° C., according to
[0128] Afterwards the printed body was cleaned and dried at 120° C.
[0129] The size of the printed sample was 13 mm×13 mm with a thickness of 2 mm. The circular inset had a thickness of 1 mm and diameter 6 mm. Debinding was performed in air at the temperature of 600° C. Sintering was performed in a vacuum furnace with tungsten heating elements at temperature 1750° C. with soaking time of 16 h. The sintered body was mirror polished and annealed in air until the Yb.sup.2+ ions, that were produced during vacuum sintering, were oxidised to Yb.sup.3+. Finally, the sample was polished with diamond pastes with grain size from 30 μm down to 0.25 μm using standard optical polishing machines.
[0130] The desired structure was obtained.