The present invention relates to the agglomeration and densification of nanoparticles powders or particles of nanometric scale sizes that can be produced by any kind of technique. More particularly, the present invention relates to densification of nanoparticles into micrometric particles.
It is well known, since its development by Benjamin et al. in U.S. Pat. No. 3,591,362, that the basic mechanism of mechanical milling, alloying or grinding, consists of a repeated deformation, fracture and cold welding by high energetic ball collisions. Depending on the dominant process during milling, such as fracturing, welding or micro-forging, a particle may become smaller through fracturing or may grow through agglomeration. This process has been extensively used for particle size reduction or growth, shape change, solid-state alloying or blending, modifying, changing or altering properties of material like the density or flowability, mixing or blending of two or more materials and agglomeration. The following patents are examples of issued patents which disclose methods of producing mechanically alloyed composite powders and consolidated products: U.S. Pat. Nos. 3,591,362; 3,660,049; 3,723,092; 3,728,088; 3,738,817; 3,740,210; 3,785,801; 3,809,549; 3,737,300; 3,746,581; 3,749,612; 3,816,080; 3,844,847; 3,865,572; 3,814,635; 3,830,435; 3,877,930; 3,912,552; 3,926,568; and 4,134,852.
Ball-milling has also been used to produce nanocrystalline materials with a structure having a large number of grains and grain boundaries, within particles globally in the micrometer scale size. In the literature, there are a large number of scientific papers attesting the capability of this technique to do so. Nanostructured materials can also be obtained by methods that do not involve ball-milling. These methods include DC and RF plasma processes, vapor-phase reactions, sol-gel techniques, combustion, emulsion and laser or hydrothermal synthesis. All these techniques produce mainly nanostructured materials with nanometer sized particles, bonded together by Van der Waal's electrostatic forces (a soft agglomeration) and present a very low density.
One of the primary limitations with nanoparticles is that nanoscale particles cannot be processed directly in many applications such as thermal spraying because of the extremely low density and flowability. Thus, there is a vital need for densifying and consolidating by agglomeration such particles into micrometer scale to enable processing. Usually, agglomeration of powders is achieved via spray drying, fluid bed agglomeration, or granulation. As a drawback, these processes often require an organic binder to ensure particle adherence, which may remain after agglomeration. There is also a risk for powder to react with the agglomeration media to form undesirable species such as oxides.
Ball milling has been used to produce powders for different applications. However, it is believed that the use of ball milling to agglomerate nano-sized particles into micrometric-sized particles has not been previously proposed. This is also believed for association of two different techniques, namely, production of nanostructured powders of a nanoscale particle size, and agglomeration of the nanoscale powders into nanostructured micrometric powders with a relatively high density.
In U.S. Pat. No. 5,631,044, issued to Rangaswamy et al., there is disclosed an improved method utilizing a high energy ball mill for preparing binder-free clad powders. The powders are indicated to be useful as thermal spray powders. It is stated that the binder-free clad powders have a core material with a particle size range of about 10 to 200 microns. These are coated or partially coated with a second material, significantly smaller than the particle size of the core material with a particle size ranging from 0.1 to 20 microns. At least one of the two materials must be deformable within the high energy ball mill. The processing time is less than about one hour. The result is a thermal spray powder having an average particle size from about 10 to 150 microns.
In U.S. Pat. No. 4,749,545, issued to Begg et al., a method is discussed which allows preparation by ball milling of composite particles made of hard material such as SiC and a matrix of aluminum or magnesium. The former material has a particle size less than 50 microns while the second is less than 100 microns. The method enables mixing of a high proportion of hard materials to be incorporated into the composite.
Similar to the previous patent, in U.S. Pat. No. 4,818,567, issued to Kemp, Jr. et al., metallic coated particles are disclosed. The particles have a core consisting essentially of metals, metal alloys, ceramics, ceramic glasses, and a coating relatively uniformly distributed on the core. The coating comprises a relatively ductile and/or malleable metallic material selected from metals and metal alloys.
In U.S. Pat. No. 4,787,561, issued to Kemp, Jr. et al., a process involving the grinding of particles of a ductile and/or malleable material which may be metal, metal alloy, or metal-ceramic composites, with a combination of parameters and environment in a ball attritor mill was disclosed. The product is densely packed particles, having a substantially granular appearance and an aspect ratio of from greater than 1 to about 50 and a mean particle size of less than about 20 micrometers in diameter.
All the above-mentioned patents have used ball milling as a tool to coat a core material or to prepare composite materials that have a microcrystalline structure. None of these reports the use of ball milling to agglomerate and consolidate nanoparticle powders.
One object of the present invention is to provide an improved process for consolidation of nanoparticle powders.
A further object of one embodiment of the present invention to provide a method of increasing the density of nanoparticles, comprising the steps of:
providing particles of a nanometer size; and
milling said particles with milling means to consolidate particles into agglomerated particles in a micrometric size distribution in the absence of binder material.
Proposed is a technique involving binderless ball-milling of nanoparticles for a short time in air or a controlled atmosphere. The resultant powders are agglomerated into particles having a size distribution, ranging from about 1 μm to more than about 100 μm, thus enabling manipulation by standard powder handling techniques. Further, the produced micrometric particles are consolidated with a high level of densification, and hence, do not need post processing like cold compaction and sintering. Importantly, the process preserves the nanostructure crystalline nature of the agglomerated particles; grains in the consolidated product remaining within the nagnometric size scale.
The process agglomerates and consolidates without binder and with a high density, nanostructured powders that have particles in the nanometer size, produced originally by any kind of technique. The process involves milling the nanoparticles by ball milling for a short period of time. The produced nanosized particles are agglomerated into powders having a micrometric particle size distribution. The starting nanostructure particles could be composed of a ductile material or composite made from ductile and brittle materials.
A further object of one embodiment of the present invention is to provide an agglomerated particle, comprising:
a particle of a micrometric size distribution formed of compacted nanoparticles of a nanometric size distribution where said particle of micrometric size distribution includes discrete nanoparticles.
This invention allows agglomeration of nanoparticles into micrometric particles. This conditioning is very useful to convert the particles for applications like thermal spraying or any other application requiring good flowability. This is also effective for avoiding manipulation of fine particle powders that are otherwise very reactive due to their high surface area. Conveniently, the process does not increase the grain size of the agglomerated particles.
Having thus described the invention, reference will now be made to the accompanying drawings.
a) and 1b) are enlarged scanning electron microscope images (350× and 20000×, respectively), illustrating the morphologies of the copper powder, material 1 as described in Table 1;
a) and 2b) are enlarged scanning electron microscope images (50× and 350×, respectively) of the powder for material 4, described in Table 1;
a) and 3b) are scanning electron microscope cross-section images of powder for material 4, as presented in
a) and 4b) are enlarged scanning electron microscope images (50× and 350×, respectively) of the powder for material 5, described in Table 1;
a) and 5b) are scanning electron microscope cross-section images of powder for material 5, as presented in
a) and 6b) are enlarged scanning electron microscope images (50× and 350×, respectively) of the powder for material 6, described in Table 1;
a) and 7b) are scanning electron microscope cross-section images of powder for material 6, as presented in
a) and 8b) are enlarged scanning electron microscope images (50× and 350×, respectively) of the powder for material 7, described in Table 1;
a) and 9b) are scanning electron microscope cross-section images of powder for material 7, as presented in
a) and 10b) are enlarged scanning electron microscope images of the powder for materials 1 (350×) and 2 (50×) (top-corner image at 350×), respectively, as described in Table 1;
a) and 12b) are enlarged scanning electron microscope images (350× and 20000×, respectively) illustrating the morphologies of the powders, corresponding to material 3 as described in Table 1;
a) and 13b) are enlarged scanning electron microscope cross-section images at 350× fo the powder for material 9 of Table 1; and
Similar numerals employed in the specification denote similar elements.
Powder Preparation by Ball-Milling
Three powders were used in the study as starting materials: a copper powder with a nanometer size distribution from CEPC (Canadian Electronic Powders Corporation), a NanoCarb WC-12Co (88% WC and 12% Co by weight) from NanoCarb, and a WC (<1 μm) from Cerac Inc. These powders are referred as material 1, 2 and 3, respectively, as described in Table 1.
From starting powders 1 to 3, six new powder materials were generated by using ball milling. These powders are also described in detail in Table 1.
Ball milling was made with a Spex 8000 machine, using stainless steel vial and grinding balls. The ball to powder weight ratio was 10:1 and the amount of the total weight of the powder was 3 g for each milling operation. Depending on produced materials, the handling of the samples was done in a nitrogen atmosphere in a glove box or in air.
Powder Characterization
Scanning electron microscopy (SEM) micrographs were obtained with a Hitachi™ H-4700 electron microscope. The microscope was also operated in the backscattered electron mode.
X-ray diffraction measurements were carried out using a Bruker™—AXS diffractometer with Cu-Kα radiation. The average crystallite size was calculated from the full width at half maximum of the reflection peaks using a Williamson-Hall style plot [G. K. Williamson and W. H. Hall, Acta Metall. 1 (1953) 22].
According to the invention, Table 1 sets forth the description of six materials (materials 4 to 9) fabricated from the three starting original materials (materials 1 to 3).
a and 1b show images obtained by SEM of the starting original copper powders. The particle has a wide particle size distribution from about 50 nm to less than about 1 micrometer. This powder, as
a and 2b are SEM identifying the morphology of material 4, which was produced after a half hour of ball milling in nitrogen atmosphere. The powder of this material has a flaky shape with a wide particle size distribution from about 10 μm to more than about 100 μm.
a and 3b are SEM cross sections of the particles described in
From this data, it has been shown that agglomeration and consolidation of the nano-sized particles into particles of micrometric size with a high level of density is achievable.
a and 6b are SEMs of the morphology of material 6, which was produced after a half hour of ball milling in air atmosphere. The powder of this material has a flaky shape with a wide particle size distribution from about 10 μm to more than about 100 μm.
a and 7b are SEM cross sections of powders, as previously shown in
a and 8b are SEM depicting morphology of material 7, which, contrary to material 6, was ball milled in air for a longer period of time, i.e. 1 h. Its particle size distribution is narrower since the difference between largest and smallest particles is smaller for material 6 than for material 7. Similar to powders of a half hour of milling, the powder in material 5, as shown in
In comparison to Example 1a, when milling is performed in an atmosphere containing sufficient oxygen, as in the case of air atmosphere tested in this example, it substantially precludes welding of particles of metallic powder to other such particles. Since generally, the less reactive the milling atmosphere, the greater the tendency for particles to agglomerate by welding. The milling atmosphere should be preferably an inert atmosphere to enhance welding of particles.
The process disclosed herein can also be used to fabricate mixtures of ductile and fragile materials.
According to the invention, cermet powders (WC-12wt. % Co), represented by material 3 in Table 1 was ball milled for 1 h under an air atmosphere to fabricate material 9.
The initial powder of material 3 is illustrated in
a is an SEM image of material 9, ball milled for 1 h under air. The particle size ranges from about a few micrometers to about more than 50 μm. This is a particle size distribution slightly different from the original starting material 3. On the other hand, as evinced by the cross section image of powder illustrated in
The grain size in the agglomerated particles following the application of the process herein described did not increase. This is supported by the data of which Table 2 presents the crystallite size calculated from the X-ray diffraction patterns presented in
The embodiment(s) of the invention described above is(are) intended to be exemplary only. The scope of the invention is therefore intended to be limited solely by the scope of the appended claims.
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Number | Date | Country | |
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20040208775 A1 | Oct 2004 | US |