The invention relates to a powder comprising granules based on zirconia and alumina, to a process for the manufacture of such granules and to a sintered part obtained from such granules.
In a sintered part based on zirconia and alumina, in particular in a part exhibiting a volume of greater than 100 cm3, the mechanical strength decreases with the amount of defects in the part and increases with the density.
There exists a continuing need for a powder which makes it possible to manufacture a sintered part based on zirconia and alumina exhibiting a volume of greater than 100 cm3, in particular for which all the dimensions are greater than 2 cm, having a good mechanical performance and a high density.
One aim of the invention is to meet this need.
The invention provides a powder comprising granules which is intended in particular for the manufacture of ceramic sintered parts, said powder exhibiting the following chemical composition by weight, based on the dry matter:
the total content of lanthanum oxide being less than 6.0%;
the median diameter D50 of the powder being between 80 and 130 μm, the percentile D99.5 being less than 500 μm and the relative density of the granules being between 30% and 60%.
Preferably, more than 80%, more than 90% and indeed even substantially 100% of the granules exhibit a composition in accordance with the composition of the powder.
As will be seen in more detail in the continuation of the description, inventors have discovered that the specific distribution in the sizes of granules according to the invention makes it possible to obtain an excellent mechanical performance, provided that the total content of the first binder, of the additional binder and of the temporary additive is limited to less than 9.0%. This is because the inventors have found that, contrary to the usual practice consisting in increasing the content of binder in proportion to the median diameter, it was advantageous, in the claimed range of median diameters, to keep the content of first binder relatively low. In particular, they have discovered that this limitation on the content of first binder limits the appearance of permanent internal defects, that is to say defects not removed during the sintering of the preform obtained by pressing said granules.
The inventors have also found that, contrary to the usual practice consisting in adding binders exhibiting high glass transition temperatures, in order to improve the mechanical strength in the green state, it was advantageous to select binders exhibiting a glass transition temperature of less than 25° C. This is because they have found that this type of binder facilitates the deformation of the granules during the pressing without, however, unacceptably reducing their mechanical strength in the green state.
The use of a binder exhibiting a low glass transition temperature is contrary to a technical preconception according to which the mechanical strength in the green state is considered to decrease with the glass transition temperature of the binder.
A powder according to the invention can also comprise one or more of the following optional and preferred characteristics:
In an advantageous embodiment, the stabilizer is chosen from the group formed by Y2O3, Sc2O3 and their mixtures and the content of said stabilizer is less than 6.5%, on the basis of the sum of ZrO2, Y2O3 and Sc2O3.
In an advantageous embodiment, the stabilizer is chosen from the group formed by MgO, CaO and their mixtures and the content of said stabilizer is less than 4%, on the basis of the sum of ZrO2, MgO and CaO.
In an advantageous embodiment, the stabilizer is CeO2 and the content of said stabilizer is greater than 10% and less than 15%, on the basis of the sum of ZrO2, Y2O3 and CeO2.
In an advantageous embodiment, the stabilizer is chosen from the group formed by Y2O3, CeO2 and their mixtures and preferably observes the relationship 10%≦3.Y2O3+CeO2≦20%, on the basis of the sum of ZrO2, Y2O3 and CeO2.
In an advantageous embodiment, the stabilizer is Y2O3, that is to say that the granules comprise only Y2O3 as stabilizer. In particular in this embodiment, the Y2O3 content is preferably greater than 3%, preferably greater than 4%, preferably greater than 4.5% and/or less than 6.5%, preferably less than 5.5%, on the basis of the sum of ZrO2 and Y2O3.
The granules can comprise stabilized zirconia, or a mixture of stabilized or unstabilized zirconia particles and of particles of said stabilizer, or a mixture of particles in which stabilized or unstabilized zirconia and said stabilizer are intimately mixed. In one embodiment, the granules comprise particles in which the stabilized or unstabilized zirconia and the stabilizer are intimately mixed. Preferably, the granules comprise particles in which the zirconia is stabilized, that is to say that the stabilizer is in solid solution in the zirconia particles. Preferably, the granules comprise particles in which the stabilized zirconia and alumina are intimately mixed.
In a first specific embodiment, the stabilizer is Y2O3, the content of stabilizer is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of lanthanum oxide is greater than 0.2% and less than 0.8%, preferably substantially equal to 0.5%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a second specific embodiment, the stabilizer is Y2O3, the stabilizer content is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of additional binder is between 0.5% and 2%, preferably between 0.5% and 1%, as percentage by weight based on the dry matter, the content of lanthanum oxide is greater than 0.2% and less than 0.8%, preferably substantially equal to 0.5%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a third specific embodiment, the stabilizer is Y2O3, the stabilizer content is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of additional binder is between 0.5% and 2%, preferably between 0.5% and 1%, as percentage by weight based on the dry matter, the content of temporary additive is between 0.5% and 1%, as percentage by weight based on the dry matter, the content of lanthanum oxide is greater than 0.2% and less than 0.8%, preferably substantially equal to 0.5%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a fourth specific embodiment, the stabilizer is Y2O3, the stabilizer content is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a fifth specific embodiment, the stabilizer is Y2O3, the stabilizer content is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of additional binder is between 0.5% and 2%, preferably between 0.5% and 1%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a sixth specific embodiment, the stabilizer is Y2O3, the stabilizer content is between 4.5% and 5.5%, as percentage by weight on the basis of the sum of ZrO2 and Y2O3, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of additional binder is between 0.5% and 2%, preferably between 0.5% and 1%, as percentage by weight based on the dry matter, the content of temporary additive is between 0.5% and 1%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a seventh specific embodiment, the zirconia stabilizer is CeO2, the stabilizer content is between 10% and 15%, as percentage by weight on the basis of the sum of ZrO2 and CeO2, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In an eighth specific embodiment, the zirconia stabilizer is a mixture of Y2O3 and CeO2, the Y2O3 content is between 1% and 2%, as percentage by weight on the basis of the sum of ZrO2, Y2O3 and CeO2, the CeO2 content is between 11% and 13%, as percentage by weight on the basis of the sum of ZrO2, Y2O3 and CeO2, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
In a ninth specific embodiment, the zirconia stabilizer is a mixture of Y2O3 and CeO2, the Y2O3 content is between 1% and 2%, as percentage by weight on the basis of the sum of ZrO2, Y2O3 and CeO2, the CeO2 content is between 11% and 13%, as percentage by weight on the basis of the sum of ZrO2, Y2O3 and CeO2, the alumina content is greater than 15% and less than 25%, preferably substantially equal to 20%, as percentage by weight based on the dry matter, the content of additional oxide, preferably of a manganese oxide, is between 0.3% and 2%, as percentage by weight based on the dry matter, the content of first binder is between 2.5% and 4%, as percentage by weight based on the dry matter, the content of impurities is less than 0.5%, preferably less than 0.1%, as percentage by weight based on the dry matter, and the residual moisture content is between 0.2% and 1%, preferably between 0.2% and 0.6%, as percentage by weight on the basis of the wet powder.
Preferably, a powder according to the invention is manufactured by spraying a slip, preferably according to a process comprising stages a) to d) described below.
Such a process advantageously makes it possible to manufacture granules exhibiting a relative density of less than 60%, indeed even of less than 50%.
The invention also relates to a process for the manufacture of a sintered part comprising the following stages:
The invention also relates to a preform obtained by the implementation of a process comprising at least stages A) and B), indeed even C), of a manufacturing process according to the invention.
The invention also relates to a ceramic sintered part obtained by sintering a preform, optionally machined, according to the invention. In particular, all the dimensions of the sintered part can be greater than 2 cm.
“Comprising a” should be understood as “comprising at least one”, unless otherwise indicated.
“A first binder” (or “an additional binder”) does not necessarily correspond to just one compound but can correspond to a mixture of several compounds, each exhibiting a glass transition temperature of less than or equal to 25° C. (or greater than 25° C., respectively). Likewise, a “stabilizer” or a “temporary additive” can correspond to mixtures of several compounds each constituting a stabilizer or temporary additive respectively.
Unless otherwise indicated, all percentages are given based on the weight of the dry powder, with the exception of the percentages relating to the stabilizers. This is because the stabilizer content of an oxide is conventionally defined, by default, as a percentage by weight on the basis of the total content of said oxide and said stabilizer.
The properties of the powder can be evaluated by the characterization methods employed for the examples.
A powder comprising granules according to the invention can be manufactured by a process comprising a stage of spraying a slip. Such a process can in particular comprise the following stages:
In stage a), the starting materials are mixed in a liquid, for example distilled water, so as to form a slip.
In the slip, the content by weight of dry matter can be between 35% and 70%. The content of dry matter in the slip is adjusted so that the relative density of the granules obtained on conclusion of stage b) is between 30% and 60%. An increase in this content is generally accompanied by an increase in the relative density of the granules obtained at the end of stage b).
Preferably, zirconia and alumina are introduced in the starting charge so that the powder comprising granules according to the invention exhibits a sum of the zirconia and alumina contents of greater than 50%, preferably of greater than 60%, indeed of greater than 70%.
The zirconia introduced can be stabilized with said stabilizer. The stabilizer can also be added independently of the zirconia. In one embodiment, the zirconia can be introduced in the form of particles in which stabilized or unstabilized zirconia and stabilizer are intimately mixed, optionally with alumina particles.
According to a preferred embodiment, the zirconia is introduced in the form of stabilized zirconia particles, that is to say that the stabilizer is in solid solution in the zirconia particles.
In another preferred embodiment, the zirconia is introduced in the form of particles in which the stabilized zirconia and alumina are intimately mixed.
The use of particles of stabilized zirconia and/or of particles in which the stabilized zirconia and alumina are intimately mixed is in particular preferred for the specific embodiments described above.
The binders are constituents of the starting charge which make possible the agglomeration during the spraying.
Conventionally, the manufacture of granules employs binders of the PVA or PEG type; binders of PVA type or PEGs having a molecular weight of greater than 600 Da do not exhibit a glass transition temperature (Tg) of less than or equal to 25° C. The inventors have discovered that the presence of a binder exhibiting a glass transition temperature (Tg) of less than or equal to 25° C., or “first binder”, favors the deformation of the granules during the pressing and reduces the number of defects. It thus results in an improvement in the mechanical properties of the sintered part obtained from the powder according to the invention.
However, a content of first binder of less than 1% does not result in a quantifiable effect. Preferably, the first binder exhibits a glass transition temperature of greater than −30° C., preferably greater than −20° C., indeed even greater than −15° C., and/or of less than 20° C., indeed even of less than 15° C.
The first binder can be chosen from polymers. A list of such polymers is disclosed in Polymer Handbook (4th Edition), 1999; 2005, John Wiley & Sons. Preferably, the first binder is chosen from amorphous organic polymers and their blends. Preferably, the first binder is chosen from polymers based on acrylates (monomer —(CH2═CHCOO—)—), which are pure or in the form of copolymers (with styrene monomers, for example), and their blends. The polymer can thus be an acrylic resin. Preferably, the first binder is chosen from polymers based on pure acrylates (monomer —(CH2═CHCOO—)—), copolymers based on acrylates (monomer —(CH2═CHCOO—)—) and styrene (monomer —(C8H8)), and their blends.
Preferably, the first binder is chosen from organic polymers exhibiting, after curing, a breaking strength of greater than 1 N/mm2, indeed even of greater than 5 N/mm2, measured according to standard DIN53455.
Still preferably, the first binder is chosen from organic polymers exhibiting, after curing, an elongation at break of greater than 100%, preferably of greater than 200%, indeed even of greater than 500%, measured according to standard DIN53455.
Preferably, the first binder is chosen from polymers not comprising inorganic elements, in particular the elements from Group 1, in particular lithium (Li), sodium (Na) and potassium (K), and the elements from Group 17, in particular fluorine (F), chlorine (Cl), bromine (Br) and iodine (I). Advantageously, the content of impurities is reduced and the mechanical strength of the sintered parts produced from the powders comprising granules according to the invention is increased.
Preferably, the content of first binder is determined so as to be greater than 2%, preferably greater than 2.5%, and/or less than 8%, preferably less than 6%, preferably less than 5%, preferably less than 4%, in the manufactured powder.
The additional binder is preferably chosen from polymers exhibiting a glass transition temperature of greater than 25° C. and less than 100° C., preferably less than 80° C., preferably less than 50° C., indeed even less than 40° C., and their blends.
Preferably, the content of additional binder is less than 3%, preferably less than 2%, more preferably less than 1% and/or greater than 0.5%.
Preferably, the additional binder is a polymer not comprising inorganic elements, in particular the elements from Groups 1 and 17. Advantageously, the content of impurities is reduced and the mechanical strength of the parts produced from the granules according to the invention is increased.
Preferably, the additional binder is chosen from amorphous organic polymers and their blends. Preferably, the additional binder is chosen from compounds based on alcohols. Preferably, the additional binder is chosen from polyvinyl alcohols and polyalkylene glycols, preferably chosen from polyethylene glycols having a molecular weight of greater than 600 Da.
A temporary additive can be added during the manufacture of the granules.
The temporary additive is preferably an organic additive which, according to rules well known to a person skilled in the art, can in particular be added to facilitate the manufacture of the granules or the forming thereof.
The content of temporary additive is preferably greater than 0.5% and/or less than 1%, the total content of binder(s) and of temporary additive preferably being less than 8%, preferably less than 6%, preferably less than 5%, indeed even less than 4%, as percentage by weight based on the dry matter. Preferably, the organic additive is chosen from dispersants or surfactants, thickeners, antifoaming agents, preservatives or biocides, lubricants and their mixtures. By way of example, dispersants or surfactants can be polyacrylates or ionic or nonionic surfactants, of the family of the Dolapix products sold by Zschimmer-Schwarz or alternatively of the Darvan products or methacrylic acids sold by R.T. Vanderbilt Company. The thickeners can be acrylic acid emulsions sold by Zschimmer-Schwarz or by BASF. The antifoaming agents can be those of the range sold by Zschimmer-Schwarz. The preservatives or biocides can be quaternary ammonium salts sold by Zschimmer-Schwarz or BASF. The lubricants can be those of the range sold by Zschimmer-Schwarz.
In one embodiment, the granules comprise an additional oxide chosen from a manganese oxide, ZnO, La2O3, ZrO, BaO and their mixtures. Advantageously, the presence of a said additional oxide increases the amount of grains of elongated form present in the parts obtained after sintering and improves the mechanical performance thereof.
The additional oxide can be chosen from MnO, MnO2, Mn2O3, Mn3O4, ZnO, La2O3, SrO and their mixtures.
The additional oxide can be chosen in particular from the manganese oxides MnO, MnO2, Mn2O3, Mn3O4 and their mixtures. Preferably, the additional oxide is chosen from MnO, Mn3O4 and their mixtures.
The content of additional oxide in the powder is preferably greater than 0.2%, preferably greater than 0.3%, indeed even greater than 0.5%, and/or less than 0.5%, indeed even less than 4%, indeed even less than 3%, indeed even less than 2.5%, indeed even less than 2%, indeed even less than 1.5%, indeed even less than 1%, as percentage by weight based on the dry matter.
The powders comprising additional oxides can also be replaced, at least partially, with powders comprising precursors of these oxides, introduced in the equivalent amounts.
In one embodiment, the alumina, the sintering additive and the additional oxide can be introduced in the form of particles in which these elements are intimately mixed.
In a specific embodiment, the granules do not comprise additional oxide.
Preferably, the purity of the starting materials is determined so that the content of impurities in a powder comprising granules according to the invention is less than 1%, preferably less than 0.5%, indeed even less than 0.3%, indeed even less than 0.1%. The hafnium oxide is not regarded as an impurity.
Preferably, the impurities are oxides.
Preferably, the starting materials are chosen so that the granules do not comprise any other constituent than the zirconia, the zirconium stabilizer, the alumina, the alumina sintering additive, the additional oxide, the binders, the temporary additive, the residual moisture and the impurities.
Preferably, the powders comprising zirconia, alumina, alumina sintering additive, additional oxide and stabilizer are introduced into the slip before the optional temporary additive and binder(s).
Each of the different starting materials of the granules, in particular the powders comprising refractory oxides, preferably exhibits a median diameter of less than 50 μm, preferably less than 20 μm, preferably less than 10 μm, and/or a specific surface preferably of less than 30 m2/g, preferably of less than 20 m2/g.
At the end of stage a), the dry matter of the slip prepared preferably exhibits a median diameter of less than 1 μm, preferably of less than 0.5 μm, more preferably of less than 0.3 μm, and a specific surface of greater than 5 m2/g, preferably of greater than 6 m2/g, and/or of less than 30 m2/g, preferably of less than 20 m2/g.
To this end, in particular if the starting materials do not exhibit a suitable median diameter and/or a suitable specific surface, the slip is preferably dispersed or ground according to methods well known to a person skilled in the art, for example by passing the slip through a mill, preferably an attrition mill. This stage advantageously makes it possible to obtain good homogeneity of the different compounds of the desired powder at the end of stage a). In particular, this stage results in a substantially homogeneous distribution of the first binder in the granules of the powder.
If stage a) comprises a grinding operation, the optional additional binder and optional temporary additive, and also the first binder, are preferably introduced after this stage.
In stage b), the spraying results in particles exhibiting a low relative density of between 30% and 60%, unlike processes such as rolling granulation or drip casting, which conventionally result in high relative densities.
Preferably, the spraying is carried out such that the granules comprise residual moisture, the moisture content preferably being less than 1%, preferably less than 0.6%, and/or greater than 0.2%, as percentage by weight on the basis of the wet powder. Advantageously, a residual moisture content of greater than 0.2% contributes to the deformation of the granules under the effect of compression. However, a residual moisture content of greater than 1% can result in an increase in the number of surface defects of the preforms manufactured by pressing starting from a powder comprising granules according to the invention, for example subsequent to adhesion of said preforms to the walls of the molds used for the pressing.
More than 80% by number, preferably more than 90% by number, of the granules exhibit a sphericity index of greater than 0.6, preferably of greater than 0.7, preferably of greater than 0.8, preferably of greater than 0.9.
In stage c), the optional sieving is preferably carried out using a sieve with an opening of less than 500 μm, indeed even of less than 400 μm. Advantageously, this stage makes it possible to remove the coarsest granules, which can be of use in certain applications.
In stage d), the optional drying is preferably carried out at a temperature of between 80° C. and 110° C., for a period of time preferably greater than 2 hours.
Preferably, the process does not comprise stage d).
The inventors have found that a powder according to the invention can exhibit the following properties:
A powder comprising granules according to the invention can be employed to manufacture a sintered part according to stages A) to E).
Stage A) can comprise stages a) and b), indeed even c) and/or d).
The starting charge can be composed of a powder comprising granules according to the invention.
In an alternative form, the starting charge can comprise a powder comprising granules according to the invention and one or more other powders. Preferably, the powder comprising granules according to the invention represents at least 60%, preferably at least 75%, preferably at least 90%, preferably at least 95%, of the weight of the starting charge.
In stage B), the forming is preferably carried out by pressing, plastic injection or extrusion, preferably by pressing. Preferably, the pressing is chosen from cold pressing and cold isostatic pressing techniques.
In the case of a forming by pressing, the starting charge is poured into a mold and then subjected to a pressure preferably of greater than 80 MPa and preferably of less than 200 MPa, indeed even less than 150 MPa, so as to form a green part, or “preform”. The granules of the powder according to the invention are efficiently deformed under the effect of this pressure. The preform can then be removed from the mold.
In the optional stage C), the preform can be machined, according to any technique known to a person skilled in the art.
In stage D), the preform is sintered, preferably under air, preferably at atmospheric pressure or under pressure (hot pressing and/or hot isostatic pressing (HIP)) and at a temperature of between 1400° C. and 1600° C., preferably of greater than 1450° C. and/or of less than 1550° C., so as to form a sintered part.
Stages B) and D) can be carried out in a single stage, for example by a hot pressing.
In the optional stage E), the sintered part can be machined, according to any technique known to a person skilled in the art.
The following nonlimiting examples were manufactured according to a process comprising the above stages A) to E).
Stage A) exhibits the following stages a), b) and c).
In stage a), for each of the examples carried out, the zirconia powder, the main characteristics of which appear in table 1 below, is dispersed by microgrinding with alumina powder, the main characteristics of which appear in table 2 below.
This microgrinding is carried out in a wet bead mill (zirconia beads comprising 3 mol % of Y2O3, with a diameter of 0.8 mm) or attrition mill. After the microgrinding, the powder exhibits a median diameter of 0.3 μm. The dry matter content of the suspension is 50% by weight.
The binders, in the form of 50% by weight solutions, are subsequently added to the suspension,
The slip thus obtained is kept stirred for 12 hours.
In stage b), the slip is subsequently sprayed on an FSD Minor device sold by Gea Niro, with an inlet temperature of the sprayer of 280° C. and an outlet temperature of the sprayer of 100° C. On conclusion of stage b), a powder comprising granules is obtained.
In stage c), the powder comprising granules is sieved with a 400 μm sieve.
In stage B), and for each of the powders comprising granules obtained at the end of stage A), the following preforms were prepared:
The preforms thus obtained were not subjected to stage C).
In stage D), said preforms were sintered according to the following cycle:
In stage E), the bars intended for the 3-point bending measurements were machined to the dimensions required for carrying out this measurement (25×10×3 mm3).
The properties of the examples were evaluated according to the following methods of characterization:
the total volume being equal to the empty volume of the measurement chamber and the volume Hg 100 psi being the volume of mercury Hg introduced into the chamber in the presence of the powder at a pressure of 0.689 MPa (i.e., 100 psi).
The inventors believe that the ability to fill a mold can be evaluated by the loose packed density of the powder and by its flowability. A high loose packed density and a high flowability value correspond to a good ability to fill a mold.
Table 3 makes it possible to make the following observations:
The powder comprising granules of example 1, using the same binders as the powder of example 3, exhibits a lower loose packed density and a lower flowability value. Its ability to fill a mold is lower than those of the powders of examples 2 to 4. The manufacturing yield for parts with dimensions of 10×5×4 cm3 (volume of 200 cm3) is much lower than that obtained with the powder comprising granules of example 3, which illustrates the advantage of a median diameter D50 of greater than 80 μm.
The powder comprising granules of example 2, using binders not exhibiting a glass transition temperature of less than 25° C., does not make it possible, after pressing and sintering, to obtain a sintered part exhibiting a high density and a high modulus of rupture in 3-point bending.
The powder comprising granules of example 4 according to the invention comprises 2.5% of an acrylic resin exhibiting a glass transition temperature equal to −10° C.
The powder comprising granules of example 3 according to the invention makes it possible to manufacture, with high yields, sintered parts having a high volume and exhibiting noteworthy mechanical properties.
Of course, the invention is not limited to the embodiments given as examples.
In particular, the bulk density of a sintered part according to the invention is not limiting.
In addition, other processes than spraying can be employed to manufacture a powder comprising granules according to the invention, for example a process involving a lyophilization stage, or a process involving a fluidized bed granulation stage, or a stage of granulation using a paddle mixer.
Number | Date | Country | Kind |
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09 59578 | Dec 2009 | FR | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB2010/055992 | 12/21/2010 | WO | 00 | 9/12/2012 |