WO2010059070A1 - Ceramic powders coated with a nanoparticle layer and process for obtaining thereof - Google Patents

Ceramic powders coated with a nanoparticle layer and process for obtaining thereof Download PDF

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Publication number
WO2010059070A1
WO2010059070A1 PCT/PT2008/000040 PT2008000040W WO2010059070A1 WO 2010059070 A1 WO2010059070 A1 WO 2010059070A1 PT 2008000040 W PT2008000040 W PT 2008000040W WO 2010059070 A1 WO2010059070 A1 WO 2010059070A1
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WO
WIPO (PCT)
Prior art keywords
emulsion
detonation
coated
nanoparticles
ceramic
Prior art date
Application number
PCT/PT2008/000040
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English (en)
French (fr)
Inventor
João Manuel CALADO DA SILVA
Elsa Marisa Dos Santos Antunes
Original Assignee
Cuf-Companhia União Fabril, Sgps, S.A.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority to US13/120,036 priority Critical patent/US9512043B2/en
Priority to DK08813055.4T priority patent/DK2337821T3/da
Priority to BRPI0823165-6A priority patent/BRPI0823165A2/pt
Priority to PT88130554T priority patent/PT2337821E/pt
Priority to KR1020117008282A priority patent/KR20110084500A/ko
Priority to CA2739991A priority patent/CA2739991A1/en
Priority to EP08813055.4A priority patent/EP2337821B1/en
Priority to PL08813055T priority patent/PL2337821T3/pl
Application filed by Cuf-Companhia União Fabril, Sgps, S.A. filed Critical Cuf-Companhia União Fabril, Sgps, S.A.
Priority to PCT/PT2008/000040 priority patent/WO2010059070A1/en
Priority to ES08813055.4T priority patent/ES2460574T3/es
Priority to CN2008801312234A priority patent/CN102165021B/zh
Priority to AU2008364348A priority patent/AU2008364348B2/en
Priority to EA201100396A priority patent/EA019292B1/ru
Priority to JP2011530979A priority patent/JP5836124B2/ja
Publication of WO2010059070A1 publication Critical patent/WO2010059070A1/en
Priority to EG2011040555A priority patent/EG26472A/en
Priority to ZA2011/02811A priority patent/ZA201102811B/en

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Definitions

  • the present invention concerns ceramic powders coated with nanoparticle layers of multiple crystalline structures, thickness, adhesion grade and crystallite size and process for obtaining these coated powders.
  • the ceramic powders according to the present invention present optical, mechanical, electrical, magnetic, catalytic and of reactive prOpei'ties substantially different from those of non-coated particles, which makes them particularly attractive for a set of applications in the nanotechnology field, such as electronics - for instance in semiconductor prodtiction, the biomedicine - for instance, in cancer treatments with magnetic nanoparticles surface-coated with functionality- enhanced nanoparticles in order to adhere to specific antibodies, chemistry - for instance in photocatalysis, in the ceramics industry - such as for obtaining sintering additives, in energy applications - such as in the nanographite material deposition. onto the surface of certain materials, in order to increase its electrical conductivity.
  • the methods usually used to prepare ceramic coatings are generally divided into four categories:
  • the micro emulsion, and sol-gel deposition, techniques are examples in this process.
  • the four main steps are the following: a) The colloidal particles intended to coat form a stable dispersion in a liquid, which also comprises the coating precursors; b) These precursor deposition onto the particle surfaces by spraying, immersion or rotation; c) The particles are polymerized during the removal of stabilizers, thus producing a gel in a. continuous net ; d) The final thermal handling results in the pyrolysis removal of the organic materials, leaving a crystalline or amorphous coating.
  • the main difficulty in coating processes via wet chemistry consists of controlling de reaction speed of the coating particle formation, making it difficult to obtain uniform coatings, with high adhesions.
  • CVD chemical vapor deposition
  • the coating thickness is high, typically between 5 and 12 microns, and there is no individual particle coating, but rather a substrate that might, have several geometrical forms .
  • a gas usually a gaseous organometalic precursor, is absorbed at the substrate surface;
  • Reaction of the first gaseous precursor with a second gas forming a monolayer, the number of reaction cycles between both precursors being the factor that controls the film's final thickness.
  • Another more elaborated technique consists of the synthesis of the base particles and of the coating particles from two gaseous precursors injected at different times in a hot- wall aerosol flow reactor.
  • a key example of this technique is the coating of tita ⁇ ia particles (TiO2) with silica (SiO2) .
  • TiO2 tita ⁇ ia particles
  • SiO2 silica
  • This approach starts from a suspension of particles intended to coat, to which a cation set is added, the cations being afterwards electrochemically reduced, forming a set of nanoparticles set which are deposited at the surface of the base particle.
  • the formation and deposition of copper oxide (CuO) nanoparticles onto silica particles (SiO2) is a classical example of the implementation of this technique .
  • the projection technique wherein a dense DC'amic-tax'get comprising the coating material, is sputtered by electrons, thus depositing it almost atom by atom in a substrate, thus forming a film.
  • a dense DC'amic-tax'get comprising the coating material
  • the method proposed by the present invention consisting of the detonation of an (W/0) emulsion, to which at least a solid precursor was previously added, which decomposes during the emulsion detonation, forming the nanoparticles comprising the desired composition, quantity and crystalline structure for the coating.
  • This method presents an enormous versatility, given that it promptly allows two different preparation means of the ceramic powders coated by a nanoparticle layer: a) Synthesizing in the same (W/0) emulsion detonation step, both the ceramic powders intended to coat, as the nanoparticles that form the coating layer.
  • two reaction kinetics are used differently for the precursors thereof, the formation reaction being extremely fast for the ceramic powders and slower in the case of decomposition of the precursors, which derive the nanoparticles that compose the coating layer .
  • the process allows: a. coating ceramic powders such as oxides, carbides, nitrides, inert metals, among others, from nanometric dimension to about 500 microns; b. From the addition of different precursors to the (W/O) emulsion in stechiometric proportions and of the combination among them during the detonation reaction, obtaining coatings with oxide nanoparticles in a multiplicity of crystalline structures (binary, ternary or superior), nitrides, inert metals, carbides, sulphides, etc; c.
  • ceramic powders such as oxides, carbides, nitrides, inert metals, among others, from nanometric dimension to about 500 microns
  • the document US5855827 in its turn, describes a cyclic process of detonation for the production of micrometric and nanometric powders and their projection at high-speed in different substrates, thus obtaining coated surfaces.
  • the detonation happens in a gaseous mixture to which metals of fine granulometry are added, a suspension, being formed.
  • the process of the present invention stands out from the later due to the use of an (W/0) emulsion, in the liquid phase, to which solid precursors are added or dissolved, or still inert ceramic particles, making it possible to obtain individual particles coated with a nanoparticle layer.
  • this emulsion is added with new types of precursors, the inert ceramic particles, intended to coat and solid nanoparticle precursors, that are critical elements for its final result, the ceramic powders coated by a nanoparticle layer.
  • the document PT 104085 discloses a method for obtaining nanomaterials at low temperature (inferior to 2000 0 C), from the detonation of two (W/0) emulsions, wherein the first is to stabilize the detonation front and the second has in its composition three types of precursors: dissolved oxidants in the internal phase, miscible fuels in the external phase and metals or alloys in the solid state, that combine during detonation in order to synthesize materials of nanometric dimension.
  • the (W/0) emulsion additionally to the types of precursors already disclosed in the said document, comprises at least a precursor added to the (W/0) emulsion, in the solid state, in way to guarantee sufficiently-differentiated formation kinetics of the base particle and nanoparticles, in order to obtain a ceramic powder coated with nanoparticles.
  • the. inert ceramic particle intended to coat is directly added to the (W/O) emulsion and, unlike the precursors in the quoted document, it does not take part in the (W/0) emulsion detonation reaction, allowing the nanoparticles to deposit on its surface.
  • the (W/0) emulsion with the precursors of the nanoparticles dissolved in the (W/0) emulsion sensitized by a military explosive (RDX) .
  • RDX military explosive
  • the (W/0) emulsion besides the oxidants dissolved in its internal phase, equally referred in the sais document, requires at least a precursor added to the
  • the inert ceramic particle intended to coat is directly added to (W/0) emulsion and, unlike the precursors in the said document, it does not take part in the (W/0) emulsion detonation reaction, allowing the nanoparticles to deposit on its surface .
  • the present invention relates to ceramic powders coated with a. nanoparticle layer with different compositions and process for obtaining the same.
  • the coatings of the pi ⁇ esent invention present a multiplicity of crystalline structures, thickness of the coating layer between 5 and 150 nm, a percentage of coated surface area, among 50 to 9b%, a high adhesiveness to the support base particle, changing their properties and functionalizing the base ceramic powders, for a multiple set of applications.
  • the process for coating the ceramic powders surface with a nanoparticles layer of different crystalline structures is based on the introduction of at least: a. precursor, in the solid state or dissolved in an (W/0) emulsion that, by decomposing during detonation result in nanoparticles, that are deposited onto the base particle that is intend to coat .
  • the said emulsion intended to detonate is of the (W/O) type, being broadly used, for instance, in the production of explosive emulsions.
  • This emulsion comprises two intimately linked phases, under the action of a surfactant: the internal (aqueous) and the external (insoluble) phase.
  • the process of the present invention can comprise two different embodiments, differing not only in the formation of the base particle (A) intended to coat, but also in the introduction of the precursor (s) that originate the nanoparticles (b) , of the coating layer (Pig.l).
  • both the base ceramic particles and the coating nanoparticles are formed during the detonation of the (W/0) emulsion
  • the ceramic particles intended to coat are directly placed and homogenized in the (W/0) emulsion.
  • the precursors of the coating nanoparticles are, in the first case, added in the solid state whereas, in the second case, they are generally dissolved in the internal structure of the (W/0) emulsion.
  • both the base ceramic particle (A) and the coating nanoparticles (b) are synthesized during the (W/0) emulsion detonation step.
  • the key aspect of this variant is that the ceramic powder (A) precursors intended for coating and the nanoparticle Cb) precursors, which constitute the coating layer, present very different reaction kinetics, during the (W/0) emulsion detonation.
  • the precursors of the base ceramic particle A are part of the emulsion internal structure, being dissolved in its internal p>hase, homogeneously mixed in the external phase, or being high reactivity metals, which allows them to present an extremely fast reaction kinetics, reacting inside or immediately behind the reaction zone, which is the zone that precedes and supports the advance of the shock wave, in the classical detonation model .
  • nanoparticle solid precursors are in the form of nitrides, sulphates, carbides, chlorides etc., for they are in the solid state and the respective decomposition reactions are highly endothermic, they do not react in the reaction zone, but in a very subsequent phase of the designated Taylor zone (or gas expansion) , zone where the base particles A are already formed, once the temperatures are inferior to their melting points, thus resulting in the fact that its coalescence-based growth no longer occurs. So being, the nanoparticles (b) are deposited and coat the surface of the base particles (A) .
  • This variant presents an enormous advantage for during the stage of (W/0) emulsion detonation, both the base particles (A) , and the coating layer nanoparticles (b) are formed.
  • the appropriate control of the process variables allows obtaining not only an enormous multiplicity of base particles of different dimensions and structures, but also base nanoparticles coatings, not only of binary structures (two elements from a single precursor) , but also ternary (from two solid precursors which combine during its decomposition, reaction) .
  • a base ceramic particle with a spynel- type structure such as MgAl204, coated by nanoparticles also of MgAl204, being for such sufficient that the (W/0) emulsion contains, in its internal phase, the stechiometric quantities of salts of magnesium and aluminium dissolved and, at the same time, be also added and mixed a certain quantity of solid precursors of the same elements (magnesium and aluminium) , depending on the coating thickness intended, the precursor quantity being larger as the thickness and the percentage of coated area increase .
  • the MgAl204 base particles are formed from the reaction of the salts dissolved in the (W/0) emulsion.
  • the coalescence and growth process of the formed particles occurs, in a subsequent phase, the external solid precursors decompose and combine, thus forming the MgAl204 nanoparticles, which project and coat the MgA12O4 base particle.
  • this variant of the process for preparing ceramic powders coated with a nanoparticle layer is constituted by the following steps:
  • the components of the (W/0) emulsion are selected from the group of soluble oxidant precursors, soluble fuels, mi ⁇ cible fuels, the choice of its nature and relative ratio depending on the empiric formula, structure type and dimension of the ceramic powder (A) intended to coat .
  • Starting from the stechiometry of the chemical reaction it is possible to calculate the necessary quantity of each precursor for the formation of a given compound, and it is equally possible to estimate from the enthalpy of the chemical reaction the detonation temperature and the coalescence time of the particles. With these data it is possible to estimate the dimension of the formed particles,
  • the step for the formation of a (W/0) emulsion begins, consisting of two intimately-linked phases, under the action of a surfactant: discontinuous internal phase (aqueous) and continuous external phase (insoluble) .
  • a surfactant discontinuous internal phase (aqueous) and continuous external phase (insoluble) .
  • the internal phase of the (W./'O) emulsion is a result of the dissolution of the precursors in water, according to the composition of the emulsion selected in 1.1.1. This phase is heated up to a. temperature between (35-105 0 C) above the crystallization point of all components, in order to allow its complete dissolution, which is important to obtain a good homogeneity of the formed products.
  • the external phase of the (w/0) emulsion is obtained by mixing of the hydrocarbons or organic materials, that compose it with a surfactant appropriate to low pH values (between 2 and 5) , soft heating between 35-85°C, in order to guarantee the appropriate viscosity of the mixture at a close temperature of the internal phase, which is important to guarantee a good emulsification of the two phases required. for carrying out stable and repi'oducible detonations .
  • the (W/0) emulsion according to the present invention is obtained, by emulsification of both internal and external phases formerly prepared according to the previously described, in an emulsified matrix, and subsequently refined at about 60-150 psi, in order to obtain micelles of 1 to 10 microns so as to produce a stable emulsion, that is, a non-degradable emulsion during the mixture of the remaining precursors .
  • an organic sensibiliser such as expanded polystyrene or plastic spheres without contaminants
  • an organic sensibiliser such as expanded polystyrene or plastic spheres without contaminants
  • the addition of metals in the solid state is endorsed, with subsequent homogenization in the (W/O) emulsion.
  • the homogenization of the emulsion is fundamental to guarantee that the parameters of the detonation reaction remain stable through time and space.
  • the dimension of particle A depends on reaction temperature and coalescence time, and. latter two parameters vary according to quantity of precursors and final material produced, the reaction/detonation temperature is the result of the difference between formation enthalpies of reagents and final products.
  • the (W/O) emulsion is subsequently placed in a cartridge of cylindrical geometry, for instance, in an appropriate material for detonation, such as paper, polyethylene or other material that it is selected in order not to introduce contaminants in the synthesized materials, with a diameter which is largei" than its critical diameter (the critical diameter is the diameter from which it is possible to sustain a. detonation, being usually experimentally determined) the detonation being then started inside an appropriate chamber from a detonation system, such as a detonator, a capacitive discharge system, laser system, among others .
  • a detonation system such as a detonator, a capacitive discharge system, laser system, among others .
  • the powders are dragged by the gases resulting from the detonation reaction, inside the expansion chamber, where they are cooled and collected in. dry or wet means.
  • the first aspect refers to the placement of the ceramic powder (A) intended to coat directly in the (W/O) emulsion, instead of being synthesized according to the previously described embodiment of the invention.
  • the second aspect refers to the nanoparticle (b) precursors, which in this case are already part of the internal structure of the (W/O) emulsion and are not subsequently added in the solid state, unlike the previously described embodiment of the invention, thus allowing not only the reduction of the quantity of total solids in the final composition, but also the improvement of the (w/0) emulsion' s rhe ⁇ logy, processability and detonability.
  • the incorporation of solids in the emulsion significantly increases its viscosity, which, limits the solids % considered as possible to introduce and difficult its homogenization, this way being preferable to dissolve them in the internal phase .
  • the key step of the coating process includes the control of the system' s atmosphere type (oxidant/reducing/inert ), mainly the (W/0) emulsion detonation temperature, in order to assure two essential aspects: a) the base particle A does not decompose, for instance the carbides decompose at high temperatures into a solid oxide and they release gaseous CO 2 ; and b) no reaction in the solid state takes place between the base particle (A) and the nanoparticles (b) which compose the coating, such as for example, when one intends to coat base alumina particles, with MgO nanoparticles, the (W/0) emulsion detonation temperature should be inferior to 800 0 C, taken that a temperature above such value will result in an undesired side reaction in the solid state between the alumina and magnesium oxide, leading to the formation of another structure (spinel Mg ⁇ 12O4), in the form of a single uncoated particle.
  • the system' s atmosphere type mainly the (W
  • this embodiment of the process of the present invention in which the ceramic powder intended to coat is directly placed in the (W/0) emulsion, has a drawback in as much as the particle intended to coat has to be previously synthesized by any process, but in compensation it allows that, both the particles intended to coat and the coating nanoparticles can be more diversified including, for instance, oxides, nitrides, carbides, siilphides, noble/inert metals. It compi'ises essentially the following stages :
  • the components of the (W/O) emulsion are selected from the group of soluble oxidant precursors, soluble fuels - such as the hydrazine and urea, for the synthesis of nitrides, miscible fuels, its relative ratio being dependent on empiric formula, on the structure type, and on the desired nanocoating (b) properties (thickness, percentage of base particle coated area, adhesiveness) .
  • the selection of the precursors is accomplished as described in 1.1.1.
  • the preparation of the (W/O) emulsion is carried out as described in 1.1.2.
  • the preparation of the (W/O) emulsion external phase is carried out as described in 1.1.2.2.
  • the emulsification of the phases, for obtaining the (W/O) emulsion, is carried out as described in 1.1.2.3. 1.2.2.4-additiori of an organic sensitizer
  • the detonation of the (W/0) emulsion is carried out as described in 1.1.4.
  • the collection and treatment of the reaction products is carried out as described in 1.1.5.
  • the coatings according to the present invention intended for ceramic particles comprise a nanoparticles layer, and are based on the detonation of a (W/0) emulsion, according to the process of the present invention. Since they are obtained at simultaneously high temperatures and pressures, they pi'esent a set of peculiax ⁇ properties.
  • These particles present the following as main characteristics : a.) they are constituted by a multiplicity of chemical compound families, such as oxides, nitrides, carbides, sulphides, noble metals;
  • the X-ray diffraction is an indispensable analysis in coating characterization, once it allows identifying the compounds present in a given sample, when a particle A (base particle) is coated by a particle (B) , it means that two different compounds are identified by the X-ray diffraction. technique; when a single compound is identified, it means that the detonation reaction conditions were not the ideal for a coating formation, except when the compound of the base particle is similar to the coating compound.
  • the X-ray diffraction technique it is possible to quantify the percentage of each compound in a given sample.
  • the size value of the crystallite is determined from Scherrer equation and with the width values at half height of the most intense pick of the X-ray diffractogram . However, this technique should be complemented with the scanning electron microscopy.
  • microscopy plays a fundamental role in coating characterization, given that it allows the morphology observation of a given compound, giving way to asses whether there are individual particles or coated particles with particles of nanometric dimension. This technique further allows quantifying the dimension of the base particle as well as dimension/thickness of the nanoparticles responsible for the coating.
  • the preparation of a suspension for determining the particle size distribution can be decisive to evaluate qualitatively the adhesiveness of the nanoparticles to the base particle. If the particle size distribution is not sensitive to the intensity and time of Bonification (application of ultrasound in a. sample) , it means that the adhesion of the coating is quite intense.
  • the results of the particle size distribution should be conjugated with the SEM images, once in the SEM it is possible to evaluate the size of the base particles and coating nanoparticles, if in the particle size distribution particles with the characteristic dimension of the coating nanoparticles appear, it means that its adhesiveness to the base particle is weak, given that such link was broken with ultrasound application during the preparation of the sample suspension. For instance, in the case of an excellent adhesion of the coating to the base particle, the result of the particle size distribution shall reflect only the base particle size that should be coherent with the size observed, in the SEM.
  • FIG 1 illustrates the three steps that are part of the two processes of the present invention:
  • step 1 consists of the preparation of the (W/O) emulsion, comprising the precursors, such as dissolved salts or metals of the base ceramic particle (A) .
  • step 2 the nanoparticles solid precursor is added, which presents a slower reaction kinetics.
  • step 3 the (W/0) emulsion detonation occurs, of which a ceramic particle (A) results being coated by a nanoparticles layer (b) .
  • the first step is constituted by the preparation of the emulsion (W/0) , comprising the nanoparticles precursors (b) , as salts or soluble fuels.
  • the base ceramic particles are added (A), which are intended to coat.
  • the third step such as process I, consists of the detonation of the (W/0) emulsion of the first step, of which ceramic particles (A) coated with nanoparticles (b) result .
  • Figure 2 illustrates the subdivision of the process II, wherein depending on the temperature of the (W/0) emulsion detonation, different situations in terms of products are obtained, namely for: a) - Temperature of (W/0) emulsion detonation inferior to the reaction temperature in the solid state (Trs) , among the particles (A) and the nanoparticles (b) , resulting in base particles (A) coated by nanoparticles (b) ; b) - Temperature of (W/0) emulsion detonation superior to the reaction temperature in the solid state, among the base ceramic particles (A) and the nanoparticles (b) , it give rise to an uniform ceramic powder (non coated) , with binary, ternary or superior crystalline structure.
  • the process for obtaining ceramic powders, coated with a nanoparticle layer depends in the first place on the powder type that is intended to be coated:
  • the preparation of the internal phase the precursors are dissolved in water, according to the composition previously selected. Subsequently, the solution is heated up to a temperature (35-105 0 C) superior to the crystallisation point of the different reagents.
  • the preparation of the emulsion external phase takes place by mixing the hydrocarbons or organic materials that compose it, with a surfactant appropriate to the mixture's pH values.
  • the mixture is heated up to a temperature among
  • an organic sensitizer occurs (0,2 to 2%), such as expanded polystyrene or plastic spheres without contaminants, which is consumed in the detonation reaction and is responsible for regulating the density to a value inferior to 1,25 g/cm3 f in. order to assure the sensibility level requested, to reach a stable detonation speed.
  • the last phase for preparing the detonation composition is mixing the sensitized (W/'O) emulsion with the two precursors in the previously defined i ⁇ atios.
  • This mixture, the detonable composition is made in a mechanical stirred tank, at a very slow speed to avoid precursor friction or degradation.
  • the (W/0) emulsion is subsequently placed in a cylindrical cartridge ⁇ or presenting a different geometry, such as spherical or of plane faces) made of paper, polyethylene or any other material, with a diameter which is superior to its critical diameter and it is initiated inside an appropriate chamber from a detonator, or any other system with similar effects, such as, capacitive discharge, laser, etc .
  • the precursors are dissolved in water, according to the composition previously selected. Subsequently, the solution is heated up to a temperature (35-105 0 C) superior to the crystallization point of the different reagents.
  • the preparation of the emulsion external phase takes place through the mixture of hydrocarbons or organic materials that compose it, with a. surfactant appropriate to the mixture pH values.
  • the merge is heated up to a temperature between 35 -85 0 C.
  • an oi ⁇ ganic sensitizer is promoted (0,2 to 2%), such as expanded polystyrene or plastic spheres without contaminants .
  • the (W/0) emulsion is subsequently placed in a cylindrical cartridge (or any other geometry such as a sphere or plane faces) made of paper, polyethylene or any other material, with a diameter which is superior to its critical diameter and initiated inside an appropriate chamber starting from a detonator, or any other system with similar effects, such as capacitive discharge, laser etc.
  • the first two examples herein presented illustrate two different ways of carrying out coatings according to the method of detonating an (W/0) emulsion.
  • the preparation of the detonable composition was carried out according to the following stages: 1.1.1. Preparation of the oxidant solution. Internal phase: dissolution of 90% ammonium nitrate in 10% deraineralised water in a stirred tank at 100 0 C. 1.1.2. Preparation of the external phase: homogeneous mixture of 80% vegetable oil with 20% surfactant.
  • Emulsification of external and internal phases emulsifying in an eraulsifier appropriate to the viscosity range, the two phases obtaining an emulsified matrix.
  • sensitized W./O emulsion homogeneous mixture, in a mechanical stirred tank, 99,7% of the emulsified matrix with 0,3% expanded polystyrene, the final product being designated sensitized W/O emulsion.
  • the last phase of the composition preparation intended for detonation consists of mixing the sensitized W/0 emulsion with both precursors in the above-mentioned ratios.
  • This mixture designated detonable composition, is carried out in a mechanical stirred tank, at a very slow speed in oi'der to avoid metal friction.
  • the detonable composition was put in a paper cartridge with a 35 mm diameter and 200mm long. Subsequently detonation was carried out,. by using the electrical detonator as detonation ignition source.
  • composition comprising the following components :
  • Titania particle size inferior to 500 nanometres
  • Emulsification of the external and internal phases in an emulsifier adequate to the viscosity range, emulsifying the two phases obtaining an emulsified matrix.
  • sensitized W/O emulsion homogenous mixture, in a mechanically stirred tank, 99,5% emulsified matrix with 0,5% expanded polystyrene, the final product being designated, sensitized W/O emulsion. l.l.b.
  • the last phase for the preparation of the composition intended for detonation is mixing of the sensitized W/0 emulsion with the two precursors in the above mentioned ratios. This mixture, designated detonable composition, is carried out in a mechanically stirred tank.
  • the detonable composition was placed in a paper cartridge with a 35 mm diameter and 200mm long. Subsequently, its detonation followed, under application of the electrical detonator as a detonation ignition source.
  • Example 3 Previous Placement of the base particle in the emulsion (W/O) )
  • composition comprising the following components :
  • Emulsifying the external phase and internal phase in an emulsifier appropriate to the viscosity range, emulsifying both phases thus obtaining an emulsified matrix.
  • the last phase for preparing the composition intended, for detonation consists of mixing the sensitized W/O emulsion with both precursors following the above- mentioned ratios.
  • This mixture, designated detonable composition is carried out in a mechanically stirred tank.
  • the composition intended for detonation was placed in a paper cartridge with a 35 mm diameter and approximately 200mm long. Subsequently, its detonation followed, under application of the electrical detonator as a detonation ignition source. 3. Collecting, treating and characterizing the products The magnesium aluminate powder was collected in wet state and was dried at 100° C. Subsequently, a representative sample was subject to the following analyses: observation in SEM, X-ray diffraction and particle size analysis.

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DK08813055.4T DK2337821T3 (da) 2008-10-13 2008-10-13 Keramiske pulvere overtrukket med et nanopartikellag og fremgangsmåde til opnåelse heraf
ES08813055.4T ES2460574T3 (es) 2008-10-13 2008-10-13 Polvos cer�micos recubiertos con una capa de nanopart�culas y proceso para obtenci�n de los mismos
KR1020117008282A KR20110084500A (ko) 2008-10-13 2008-10-13 나노입자 층으로 코팅된 세라믹 분말, 및 이를 제조하는 방법
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PL08813055T PL2337821T3 (pl) 2008-10-13 2008-10-13 Ceramiczne proszki powleczone warstwą nanocząstek oraz sposób ich otrzymywania
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WO2012052923A1 (en) * 2010-10-18 2012-04-26 Innovnano - Materiais Avançados, S.A. Continuous process for nanomaterial synthesis from simultaneous emulsification and detonation of an emulsion
WO2012147449A1 (ja) * 2011-04-28 2012-11-01 第一稀元素化学工業株式会社 スピネル粉末およびその製造方法、ならびに溶射膜およびガスセンサ素子の製造方法
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AU2008364348A1 (en) 2010-05-27
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