WO2009092207A1 - A stirring device, a device with said stirring device for producing nanometer powder and its method - Google Patents

A stirring device, a device with said stirring device for producing nanometer powder and its method Download PDF

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Publication number
WO2009092207A1
WO2009092207A1 PCT/CN2008/070675 CN2008070675W WO2009092207A1 WO 2009092207 A1 WO2009092207 A1 WO 2009092207A1 CN 2008070675 W CN2008070675 W CN 2008070675W WO 2009092207 A1 WO2009092207 A1 WO 2009092207A1
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WO
WIPO (PCT)
Prior art keywords
support
deposition
stirring
agitation tank
agitation
Prior art date
Application number
PCT/CN2008/070675
Other languages
French (fr)
Chinese (zh)
Inventor
Cheolsu Lee
Seokkeun Koh
Jaeho Joo
Unjung Yeo
Original Assignee
Inano Limited
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
Application filed by Inano Limited filed Critical Inano Limited
Priority to CN2008801254116A priority Critical patent/CN101925402A/en
Publication of WO2009092207A1 publication Critical patent/WO2009092207A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/15Stirrers with tubes for guiding the material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05Stirrers
    • B01F27/11Stirrers characterised by the configuration of the stirrers
    • B01F27/17Stirrers with additional elements mounted on the stirrer, for purposes other than mixing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/90Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms 

Definitions

  • the present invention relates to the field of nanotechnology, and in particular to a stirring device, a nanopowder manufacturing device having the stirring device, and a manufacturing method. Background technique
  • Nanotechnology has become the most fundamental foundation in important technical fields such as information and communication technology (IT), life science technology (BT), and environmental technology (ET), which are called high-tech, and has great potential in the field of technology development. Influence. Nanometers (the Nano) refers to a unit equivalent to 10-9 meters, so-called nano-technology is constructed or isolated atoms and molecules and to control the operation of the constituent elements of technology. Nanotechnology is characterized by high-tech intensification, high economic spread, maximum energy efficiency, and environmental affinity.
  • Nano industry segments can be categorized as Nano Processes, Nano Structures, Nano Functions, Nano Components & Systems, Nano Infrastructures, and Nanomaterials. (Nano Materials) and so on. Nanotechnology can be applied to nano materials, nano devices, nano bios, medical, environmental, energy, nanosystems, security, etc., and has a wide range of applications. The most basic nanomaterials in the field of nanotechnology can be divided into Nano Particles, Nano Wire, Nano Tube, Nano Wall, and Nano Capsule. , Nano Rod, etc.
  • the nanopowder refers to ultrafine particles which are not in the size and shape of the particles and have an average particle diameter of 100 nm or less.
  • the manufacturing method of the nano powder can be classified into a gas phase method, a liquid phase method, and a solid phase method.
  • Representative manufacturing methods using the gas phase method include a gas evaporation/condensation method and a gas phase synthesis method, and a liquid phase method includes a precipitation method and a spray drying method.
  • the method has a mechanized pulverization method in the solid phase method.
  • the manufactured nanopowder exhibits specific electrical, magnetic, mechanical, and catalytic properties that cannot be observed in the original material due to the miniaturization of the material structure (below 100 nm) and the accompanying increase in surface area. Therefore, it can be applied to a new generation of functional materials such as magnetic components, sensors, filters, and catalysts.
  • nanoparticles produced by chemical reactions may have residual ions in many reaction processes, so aggregation between particles is likely to occur.
  • an additive such as a surfactant or a dispersant is usually used, so that the purity of the nanoparticles is relatively low.
  • the method of chemically manufacturing nanoparticles is difficult to produce quantitative nanoparticles when mixing inert metals or metal salts of different properties, so there are limitations in the material selection of the nanoparticles. Due to such problems, the method of chemically manufacturing nanoparticles reduces the original function of the nanoparticles, requiring additional costs for the treatment of oxidants, reducing agents, residual acids and the like.
  • the method of physically manufacturing nanoparticles can be divided into a Top Down method and a Bottom Up method.
  • the down-direct method is, for example, mechanically pulverizing the mass to produce nanoparticles;
  • the upward-oriented method for example, refers to the application of an energy source to the material to produce nanoparticles by evaporation/condensation.
  • a representative example of a low-level physical manufacturing method of nanoparticles is a high-energy pulverization method (High Energy Mi lling), and an example of an upward-oriented method is an inert gas condensation (IGC).
  • the upward-oriented nanoparticle production method includes thermal evaporation, E-beam evaporation, DC sputtering, DC sputtering, and RF sputtering.
  • RFS Ion Beam Sputtering
  • IBS Ion Beam Sputtering
  • MBE Molecular Beam Epitaxy
  • FAP Flame Aerosol Process
  • CVD Chemical Vapor Deposition
  • CVS Chemical Vapor Synthesis
  • Laser Ablation Laser Ablation
  • the existing physical methods for manufacturing nanopowders generally have the following problems: uneven particle size, difficulty in controlling particle size, inefficient manufacturing processes, contamination, and limitations in mass production.
  • the existing methods for physically manufacturing nanoparticles the most representative methods can be classified into mechanical pulverization, electric blasting, and Inert Gas Condensation (IGC).
  • the mechanical pulverization method is suitable for mass production, it is difficult to control the size of the nanoparticles below 100 nm, and there is a problem of contamination during the pulverization process.
  • the method of fabricating nanoparticles by electric blasting is to use a pulse power in a vacuum to produce a nanoparticle by instantaneously releasing a charged high voltage and a high current to evaporate/condense on a metal wire of a capacitor. . Since this method utilizes instantaneous blasting, there are disadvantages in that it is difficult to control the size of the nanoparticles and it is necessary to recollect the nanoparticles. Although some attempts have been made to produce nanoparticles by the same method in solution, such methods also require separation of the solution and the nanopowder, so that it is difficult to singulate the process and obtain pure nanoparticles.
  • the inert gas condensation method can produce a nanopowder of higher purity, the materials that can be used for manufacturing have limitations.
  • the inert gas condensation process requires the nanoparticles to be condensed after the cooling rods, and the condensed nanoparticles need to be recollected. If it is to be applied to the final product, it needs to be processed through additional processes, so it is not suitable for mass production.
  • the nanopowder produced by the inert gas condensation method is rapidly oxidized in the atmosphere, so it can be applied to the product immediately after being recovered in a vacuum chamber, or a small amount of oxygen is injected into the vacuum chamber to slowly oxidize the nanopowder. The surface facilitates the removal of nanopowder in air.
  • nanopowder [ 1-11] manufactured by the support is easy to take, and when the constituent material of the final product is used as the support, the manufacturing process can be simplified.
  • the nano-powder manufacturing devices suggested in the existing patents or papers have low deposition efficiency, wide nano-particle size distribution, uneven support agitation, excessive load on the support, and durability of the device. Low question.
  • the support is unevenly stirred.
  • the durability of the equipment is low, the overload of the agitating structure, and the pulverization of the support due to the load between the supports.
  • a support to produce a uniform and stable nanopowder is important for discontinuous deposition, i.e., controlling the time and non-deposition time of nanomaterial deposition on the support.
  • the deposition time By appropriately controlling the deposition time to prevent excessive growth of the nanoparticles, the nanoparticles tend to be stable during the non-deposition time, and even if exposed to the deposition area, the nanoparticles do not continue to grow, forming other nuclei on the support.
  • the support must be uniformly agitated.
  • deposition sources have been used in the industrial field (for example, using resistance heating, induced heating, plasma jet, electron beam, laser beam deposition source, and ion beam sputtering, DC (Direct Current) sputtering.
  • a deposition source such as RF (Radio Frequency) sputtering or Electron Cyclotron Resonance (ECR) is applied to a nanoparticle production apparatus to produce a variety of materials such as metals, ceramics, oxides, and organic materials into nanoparticles.
  • RF Radio Frequency
  • ECR Electron Cyclotron Resonance
  • Fig. 1 and Fig. 2 show an example of a stirring device of a horizontal axis stirring method. Due to the rotation of the agitation tanks 130, 230, the support materials are brought together in one direction, so that the support material cannot be uniformly stirred.
  • the agitating device shown in Fig. 1 has a structure in which the agitating tank 130 rotates in the main body, and adopts a drum-type horizontal axis rotating type stirring structure, and the deposition source 111 is located inside the rotating tub.
  • Fig. 1 the drum is rotated in one direction 131.
  • the support body 120 cannot be completely stirred during the stirring process, and the rotating drum and the support material slide with each other, and some powders may not be stirred. In particular, the slippage between the cohesive support and the agitation tank is more serious.
  • the deposition source is located inside the rotating drum, so if a small or low density support material is used, the deposition source is highly likely to be contaminated.
  • Fig. 2 shows a stirring structure of a horizontal shaft rotating mode in the stirring device, the stirring tank 230 is fixed, and the deposition source 211 is located outside the stirring tank.
  • Fig. 2 is also the same as the apparatus of Fig.
  • the respective rotating shafts are rotated in a certain direction, and the support material is moved in the same direction, so that the effect of being unable to uniformly stir can not be achieved.
  • the random rotation of the agitator shaft causes friction between the support materials, which is caused by the instantaneous rotation of the rotating shaft direction, resulting in irregular movement of the support material, uneven support agitation, loss of the support material, and durability of the device. Reduce and many other issues. In the manner in which the nanoparticles are fabricated using the support material, continuous movement and uniform agitation of the support material are important.
  • the rapidly changing direction of rotation causes the agitating structure to force the support material, causing severe comminution of the support particles or the support material being instantaneously blown to the outside.
  • the disadvantage of these devices is that heat is generated by random agitation, so that a heat-resistant support material cannot be used.
  • the pulverization of the support material forms fine particles, thereby generating dust.
  • the support body flows out of the agitation tank and flows into the vacuum exhaust pipe, the support material will contaminate the vacuum pump, shorten the repair/maintenance period, generate additional repair/maintenance costs, and reduce the production efficiency of the product.
  • the rapid change of the direction of rotation switches a strong external force on the rotating part, reducing the durability of the device.
  • control layer such as the size, content, and distribution of the nanoparticles
  • the support material cannot be stably and uniformly stirred, it is difficult to produce nanoparticles of a certain size. On the whole, most of the nanoparticles formed are more likely to be of different sizes.
  • Figures 3 and 4 show an example of a stirring device that detaches the horizontal rotating shaft structure to produce nanoparticles.
  • the apparatus shown in Fig. 3 can be regarded as a stirring mode similar to that of Fig. 1, except that the rotating shaft of the stirring tank 330 has an angle from the horizontal, and the deposition source 311 is moved from the inside of the stirring tank to the outer position.
  • a device such as that of FIG. 3 has difficulty in securing a deposition area, so there is a problem in the efficiency of deposition and the fabrication of a large-capacity device.
  • Fig. 1 shows an example of a stirring device that detaches the horizontal rotating shaft structure to produce nanoparticles.
  • the apparatus shown in Fig. 3 can be regarded as a stirring mode similar to that of Fig. 1, except that the rotating shaft of the stirring tank 330 has an angle from the horizontal, and the deposition source 311 is moved from the inside of the stirring tank to the outer position.
  • a device such as that of FIG. 3 has difficulty in
  • Fig. 4 is an example of a stirring device in which a stirring shaft adopts a vertical stirring configuration.
  • Such a device is a very effective method for agitating a solution phase material, but when stirring a solid powder or chip or the like in a solid form, in order to mix the support materials at the upper and lower positions, it is necessary to increase the stirring blade.
  • When the speed of the stirring wing is increased not only the mixing efficiency of the upper and lower materials cannot be achieved, but the material surrounding the rotating wing may be crushed by external force. Therefore, such a configuration can be regarded as a pulverizing device which is more suitable as a stirring device than a support material.
  • Another object of the present invention is to provide a nanopowder manufacturing apparatus for producing a nano powder having a uniform size.
  • the present invention also provides a method of producing a nanopowder to produce a nano powder of uniform size.
  • an embodiment of the present invention provides a stirring device, the stirring device comprising: a stirring tank for supporting a nano material;
  • a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
  • a support plate located in the agitation tank and at the upper portion of the vertical conveying member for supporting the vertical conveying
  • an embodiment of the present invention further provides a nano powder manufacturing apparatus, the apparatus comprising:
  • a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
  • the apparatus includes a deposition source located in the agitation tank and above the support plate for depositing the nanopowder to the support by physical deposition.
  • an embodiment of the present invention further provides a method for manufacturing a nano powder, the method comprising:
  • a loading step for loading the support into the agitation tank and performing deposition source material installation, wherein the agitation tank and the deposition source are disposed in a vacuum chamber in an atmospheric state;
  • a stirring and deposition step stirring the support body by means of stirring of a spiral vertical conveying support, and depositing a nano powder by a physical deposition method to a support in a deposition area while stirring;
  • the nanopowder acquisition step breaks the vacuum in the vacuum chamber, and the nanopowder attached to the support is obtained from the agitation tank.
  • the nanopowder attached to the support can be processed later or applied directly to the application product.
  • the nanoparticle manufacturing device of the embodiment of the invention adopts a spiral vertical conveying type support body stirring device to minimize the mechanized load and transport the support body with a certain speed and direction, thereby achieving uniform stirring and improvement of the support body.
  • the deposition efficiency, thereby producing a certain size of nanoparticles, while realizing the mechanical load and the load of the device are minimized, and the nanoparticle manufacturing device for improving the durability of the device is realized.
  • FIG. 1 is a schematic view of a stirring device using a horizontal axis rotation method in the prior art
  • FIG. 2 is a second schematic view of a stirring device using a horizontal axis rotation method in the prior art
  • FIG. 3 is a schematic view of a stirring device using a tilting shaft rotation mode in the prior art
  • FIG. 4 is a schematic view of a stirring device using a vertical rotation mode in the prior art
  • FIG. 5 is a schematic structural view of a nanopowder manufacturing apparatus adopting a vertical conveying method according to an embodiment of the present invention
  • FIG. 6 is a schematic view of an upper support support plate and a spreader according to an embodiment of the present invention.
  • FIG. 7 is a simplified example of the structure of a nanopowder manufacturing apparatus in an embodiment of the present invention.
  • TEM 8 is an example of a transmission electron microscope (TEM) image of a silver nanoparticle manufactured by using an existing nano powder manufacturing apparatus
  • Fig. 9 is a TEM image example of silver nanoparticles prepared by the nanopowder manufacturing apparatus of the present invention
  • Figs. 10a and 10b are schematic diagrams showing the distribution of silver nanoparticles prepared by the nanopowder manufacturing apparatus according to the present invention. detailed description
  • Embodiments of the present invention provide a support stirring device and a nano powder manufacturing device for nano powder manufacturing.
  • Fig. 5 is a schematic view showing the structure of a nanopowder manufacturing apparatus adopting a vertical conveying method in the embodiment of the present invention
  • Fig. 7 is a more specific example.
  • the nano powder manufacturing apparatus of this embodiment includes:
  • a support agitating device comprising: a stirring tank, a vertical conveying member, a support plate 534, And one or more upper rotors (or spreaders) 532;
  • a deposition device comprising a deposition source located above a support plate of the agitation device for depositing a nanopowder to the support by physical deposition;
  • a vacuum chamber for accommodating the deposition source and the stirring device, wherein the vacuum chamber is maintained in a vacuum state so that the deposition source and the stirring device are in a vacuum;
  • a vacuum pump is connected to the vacuum chamber for vacuuming the vacuum chamber to maintain a vacuum in the vacuum chamber.
  • the vacuum degree in the vacuum chamber can be controlled at 5 X 10 -1 Torr to 1 X 10 -6 Torr as needed, but is not limited thereto.
  • a heating device 536 may be provided outside the agitation tank to heat the support in the agitation tank.
  • a cooling device 536 may be provided outside the agitation tank to cool the support in the agitation tank. It is also possible to provide heating and cooling means at the same time to decide whether to open the heating or cooling device as needed.
  • the vertical conveying member is located in the agitation tank 530 for vertically conveying the support body 520 from the lower portion of the agitation tank to the upper portion of the agitation tank.
  • the vertical conveying member further includes: a rotating shaft and a fixed A spiral rotor on the rotating shaft.
  • the vertical conveying member may also be referred to as a spiral main rotating shaft 531 or a spiral bolt.
  • the support plate 534 is located at an upper portion of the vertical conveying member for supporting the support body conveyed by the vertical conveying member, and the support plate is preferably disposed in the middle (close to rotation) in order to facilitate the sliding of the support body on the support plate.
  • an outer circumference of the spiral main rotating shaft 531 may be provided with a separating cylinder, and an upper portion of the cylinder may be integrally or fixedly connected with the supporting plate, and a gap between the lower portion of the cylinder and the bottom of the stirring tank may be The support is moved to the main rotation shaft through the gap, and the support is moved to the upper portion of the agitation tank by the rotation of the spiral rotor.
  • the length of the spacer cylinder can also be set shorter, such as only enclosing the upper portion of the spiral main rotating shaft to expose the lower portion.
  • the support plate and the isolation tube can be fixed in the agitation tank by various existing methods (such as by a bracket or the like), and will not be described in detail herein.
  • the one or more upper rotors (or spreaders) 532 are located on the support plate for agitating the support on the support plate.
  • the support on the support plate is moved to the edge of the support plate and dropped into the agitation tank when it is dropped.
  • the deposition material to be deposited on the deposition source may use noble metals or oxides such as gold, silver, platinum, rhodium, ruthenium, palladium, iridium, osmium, etc., organic compounds, alloys, common metals (such as aluminum A1), bismuth (Se), silicon ( Materials such as Si) and germanium (Ge) are used as deposition materials for deposition sources.
  • noble metals or oxides such as gold, silver, platinum, rhodium, ruthenium, palladium, iridium, osmium, etc.
  • common metals such as aluminum A1
  • bismuth (Se) bismuth
  • silicon Materials such as Si
  • germanium (Ge) germanium
  • the deposition material does not have conductivity
  • RF sputtering, ion beam sputtering, or the like may be employed, but In this connection, intermediate frequency sputtering, microwave deposition, double magnetic sputtering, thermal deposition, electron beam deposition, laser deposition, electron cyclotron resonance or ion plating may also be employed.
  • the support material moves with the inclined surface of the support plate 534, thereby achieving uniform agitation. The support moved to the edge of the support plate is dropped into the support agitation tank to obtain a stabilized non-deposition time for the nanoparticles deposited on the support.
  • holes 612 are drilled in the support plate (as shown in Figure 6) to allow the support to fall quickly from the support plate, thereby controlling the support exposure time and thereby controlling the deposition.
  • Controlling the support exposure time in the deposition zone essentially means adjusting the ratio of non-deposition time to deposition time to achieve control of the nanoparticle size of the support surface.
  • the lower portion is made smaller than the upper portion (i.e., the upper portion is thicker and thinner).
  • At least one lower rotating wing 533 is also installed in order to uniformly agitate the lower support (each layer may be different in angle from the main rotating shaft, and two or more rotating wings may be provided in each layer).
  • the upper rotary wing and the lower rotary wing may be fixed to the spiral main rotation shaft 531 (but are not limited thereto).
  • the support material moved to the agitation tank 530 is slowly moved to the lower part of the agitation tank as the lower rotary wing 533 is continuously stirred, and moved
  • the support moved to the main rotating shaft 531 is moved to the upper portion of the stirring tank again by the rotation of the bolt. Repeatedly doing such a process, the nanoparticles supplied by the deposition source adhere to the surface of the support in the form of a powder or chip.
  • the agitator structure of the present invention is constituted by a main-rotation shaft for conveying a support of a spiral type, an auxiliary agitating blade for upper agitation, an auxiliary agitating blade for agitating a lower support body, and the like, and a helical rotary shaft 531 adopting a vertical transfer method.
  • a structure in which the upper support agitating portion 532 is not exposed to the deposition source is formed, that is, the upper rotary wing is buried on the support plate. In the support body.
  • the nanoparticle manufacturing apparatus having the above-described agitator structure according to the embodiment of the present invention has a uniform stirring property of the support material and a deposition efficiency in the deposition region, compared with the conventional support stirring method.
  • the advantage of preventing the pulverization of the support or the like since the external force applied to the support is minimized during the stirring process.
  • the nanoparticle manufacturing device of the embodiment of the invention minimizes the pollution of the vacuum pump and the load of the stirring shaft, reduces the maintenance cost of the equipment, and improves the durability of the equipment.
  • the nanoparticle manufacturing apparatus can easily manipulate the surface area of the support volume when compared with the deposition area in the control of the nanoparticle, and can easily adjust the ratio of the deposition time to the non-deposition time, and is generally easy to adjust the nanoparticle. size.
  • the nanopowders produced by the nanopowder manufacturing apparatus of the present invention may have an average size ranging from 1 nm to 500 nm, and the nanopowder deposited on the support may be in the range of 1 ppm to 10, OOO ppm.
  • the process flow of the nanoparticle manufacturing apparatus of the embodiment of the invention is divided into selecting a nano material and a support material, loading a nano material and a support material in a loading stage, a vacuum exhaust stage, a nano powder manufacturing (stirring/depositing) stage, and breaking The vacuum stage, the stage of taking out the nanopowder and the support material.
  • the surface of the support may be pretreated in advance using physical or chemical methods commonly used in the prior art.
  • the nano material ingot is mounted on the deposition source, and the support material is charged into the stirring tank.
  • the vacuum exhaust stage the first vacuum is started by the low vacuum pump under atmospheric pressure, and after the appropriate vacuum is reached, the high vacuum pump is used. The second vacuum is exhausted.
  • the support material contained in the agitation tank may be stirred by a stirrer.
  • a heating device (536) as shown in Fig. 5 may be provided outside the stirring tank.
  • the temperature in the vacuum chamber can be lowered by installing a cooling device (536), thereby reducing the degree of support.
  • a process of growing nanoparticles on the support by the deposition source is entered.
  • the stirring method of the spiral type vertical conveying support body is adopted, and the bottom and upper support bodies can also be assistedly stirred.
  • the nanomaterial supplied from the deposition source grows on the support material into nanometer-sized particles.
  • the particles deposited on the support are exposed to the deposition source, the particles will grow, and the nanoparticles of a certain size will move from the exposed field to the inside of the stirred tank with the stirring of the support.
  • the nanoparticles moving into the inside of the agitation tank are stabilized again before the support is exposed to the deposition field, and a certain size of nanoparticles is formed. If the nanoparticles are exposed to the deposition area before stabilization, the nanoparticles will grow more and are likely to grow into very large nanoparticles.
  • the size of the nanoparticles formed on the support can be adjusted by adjustment of deposition time and non-deposition time. In the stirring/deposition process, the ratio of the deposition rate (Deposition Rate), the deposition time, the deposition time to the non-deposition time (related to the inclination of the support plate, the number and size of the holes on the support plate), and the stirring speed can be adjusted.
  • the size and content of the nanoparticles are controlled by conditions such as the temperature of the evaporation source, the temperature of the support, the degree of vacuum, the ratio of the total surface area of the support exposed to the deposition area to the volume of the total support, and the like.
  • the main improvement lies in the manner of stirring of the support.
  • the vacuum in the vacuum chamber is broken, and the support to which the nanopowder is attached is taken out from the stirring tank.
  • a further advantage of the nanopowder manufacturing process according to the present invention is that if the material of the final application product structural material is selected for use as a support material, the process can be simplified, and since it is not added with other additives, it is environmentally friendly. , and can maximize the inherent properties of nanopowders.
  • 8 and 9 are transmission electron microscopes (TEM) of silver nanopowders produced by a nanopowder manufacturing apparatus using a conventional horizontal rotating shaft and a nanopowder manufacturing apparatus having a vertical transfer rotating shaft of the present invention, respectively. Image example. As is apparent from Figs. 8 and 9, the distribution of the nanoparticles produced by the nanoparticle production apparatus of the present invention is more uniform.
  • Fig. 10a and Fig. 10b show examples of the size distribution of the nanopowders produced by the conventional nanopowder manufacturing apparatus and the apparatus for producing nanopowder of the present invention, respectively.
  • Figure 10a compares the size distribution of nanopowders at 2-30 nm
  • Figure 10b compares the size distribution of nanopowders above 10 nm.
  • A represents silver nanoparticles produced by a conventional stirring method
  • B represents silver nanoparticles produced by the stirring method of the present invention.
  • Figures 10a and 10b show the results of the relative transformations based on the largest number of particle sizes (i.e., the peaks of the two curves are normalized). As shown in Figs.
  • the mixer using the vertical conveying method can achieve uniform agitation and suppress the formation of large nanoparticles.
  • Nanopowder 8 to 10a and 10b illustrate the nanopowder prepared by the present invention by taking silver nanopowder as an example, but the present invention is not limited thereto.
  • nano powders of other materials can also be prepared, and other metals (such as gold, platinum, rhodium, ruthenium, palladium, iridium, ruthenium, etc.) and oxides can be prepared as well.
  • Nano-powders of materials such as organic compounds, alloys, and semiconductors (such as Se, Si, and Ge).
  • the nanoparticles below 10 nm can account for 89.9% of all the nanoparticles, and the nanoparticles above 10 nm account for 10.1% of all the nanoparticles.
  • the nano-powder produced by the vertical transport method according to the present invention the nano-powder of metal or other materials (such as oxide, organic, alloy, Se, Si, Ge, etc.) can be adjusted by adjusting the appropriate experimental conditions. The following indicators can be achieved: Nanoparticles below 10 nm account for 90% to 96.1% of all nanoparticles, and nanoparticles above 10 nm account for 3.9% to 10% of all nanoparticles.
  • nano-powder can control the production of nano-powder to meet the predetermined indicators, for example, can control the production of nano-powder, so that nanoparticles below 10 nm account for 91%, 93%, or 96%, etc., and / or more than 10 nm
  • the nanoparticles account for 5%, 6%, or 8% of all the nanoparticles, but are not limited thereto.
  • the nanoparticle production apparatus of the present invention is formed by a process of depositing nanoparticles on a powder or a chip as a supporter by a physical deposition method as exemplified above.
  • the invention adopts a continuous deposition method to control the growth of nanoparticles, and has an effective device for controlling the size and content of mass production of nano powder.
  • the present invention is an excellent nano-powder manufacturing apparatus which enhances deposition efficiency and durability by a highly efficient support body stirring method compared with the existing support body stirring method.
  • the nanoparticle production method used in the present invention belongs to an upward physical physical method nanoparticle production method for forming nanoparticles in a vacuum.
  • the nanoparticle manufacturing device of the invention adopts a spiral vertical conveying mode support body stirring mode to minimize the mechanized load and transport the support body with a certain speed and direction, thereby achieving uniform stirring of the support body and improving deposition efficiency.
  • a nanoparticle manufacturing apparatus that achieves mechanical load and equipment load minimization and improves equipment durability is realized.
  • the stirring method adopts a method of conveying the support powder or the chip in a vertical manner to minimize the friction between the support or the support chip, and uniformly mix the nano particles.
  • Efficiency and durability of nanoparticle manufacturing equipment are related inventions suitable for mass production equipment.
  • the present invention is a process of agitating a support powder or a chip in a vacuum while further including depositing a nanomaterial on a powder or a chip by a deposition device.

Abstract

A stirring device, a device with said stirring device for producing nanometer powder and its method are provided. The device for producing nanometer powder includes a stirring tank (530) for containing supporters (520) of nanometer material, a vertical transportation part (531) located in the stirring tank (530) for transporting said supporters (520) from lower portion to upper portion of the stirring tank (530) by helical rotation, a support plate (534) located in the stirring tank (530) and at upper portion of the vertical transportation part (531) for supporting supporters (520) from said vertical transportation part (531), said support plate (534) is cone-shaped or frustum of a cone in shape of which central section is higher and circumference section is lower, and a depositing device including a depositing source located in the stirring tank (530) and above the support plate (531) for depositing nanometer powder on the supporters in manner of physics disposition. The device for producing nanometer powder can mix the supporters or supporter chips uniformly and reduce the friction between supporters or supporter chips.

Description

搅拌装置、 具有搅拌装置的纳米粉末制造装置及制造方法 本申请要求 2008年 1月 22日提交的中国专利申请 No. 200810004352. 9的优先 权, 现将中国专利申请 No. 200810004352. 9的全部内容以引用的方式合并于此。  Agitating device, nano powder manufacturing device with agitating device, and manufacturing method. The present application claims priority to Chinese Patent Application No. 200810004352, filed on Jan. 22, 2008, the entire contents of the Chinese Patent Application No. 200810004352. Incorporated here by reference.
技术领域 Technical field
本发明涉及纳米技术领域, 具体的讲, 涉及一种搅拌装置、 具有搅拌装置 的纳米粉末制造装置及制造方法。 背景技术  The present invention relates to the field of nanotechnology, and in particular to a stirring device, a nanopowder manufacturing device having the stirring device, and a manufacturing method. Background technique
纳米技术在被称为高新技术的信息通信技术 (IT)、 生命科学技术 (BT)、 环 境技术 (ET)等重要的技术领域中, 成为最根本的基础, 并且对技术开发领域有 着极大的影响力。 纳米(Nano)是指相当于 10— 9米的单位, 所谓纳米技术是指隔 离原子和分子构造或控制并操作组成因素的技术。 纳米技术的特点在于高技术 集约度、 高经济波及性、 能源效率的最大化、 环境亲和性等方面。 Nanotechnology has become the most fundamental foundation in important technical fields such as information and communication technology (IT), life science technology (BT), and environmental technology (ET), which are called high-tech, and has great potential in the field of technology development. Influence. Nanometers (the Nano) refers to a unit equivalent to 10-9 meters, so-called nano-technology is constructed or isolated atoms and molecules and to control the operation of the constituent elements of technology. Nanotechnology is characterized by high-tech intensification, high economic spread, maximum energy efficiency, and environmental affinity.
纳米的产业领域可分类为纳米工程(Nano Processes)、 纳米结构(Nano Structures)、 纳米功會 (Nano Functions)、 纳米元件禾口系统(Nano Components & Systems)、 纳米基础 (Nano Infrastructures)以及纳米材料 (Nano Materials) 等。纳米技术可应用于纳米原材料(Nano Materials)、纳米元件(Nano Devices)、 纳米生物 (Nano Bio) , 医疗、 环境、 能源、 纳米系统、 安全等领域, 应用范围 极为广泛。在纳米技术领域中最基本的纳米材料,按形状可分为纳米粒子 (Nano Particles)、纳米线 (Nano Wire)、纳米管 (Nano Tube)、 纳米壁 (Nano Wall) , 纳米胶囊 (Nano Capsule)、 纳米棒(Nano Rod)等。  Nano industry segments can be categorized as Nano Processes, Nano Structures, Nano Functions, Nano Components & Systems, Nano Infrastructures, and Nanomaterials. (Nano Materials) and so on. Nanotechnology can be applied to nano materials, nano devices, nano bios, medical, environmental, energy, nanosystems, security, etc., and has a wide range of applications. The most basic nanomaterials in the field of nanotechnology can be divided into Nano Particles, Nano Wire, Nano Tube, Nano Wall, and Nano Capsule. , Nano Rod, etc.
纳米粉末是指不在于粒子的大小与形状,平均粒径在 lOOnm以下的超细颗粒。纳 米粉末的制造方法可分为气相法、 液相法及固相法。 利用气相法的代表性制造 方法有气体蒸发 /凝缩法和气相合成法, 液相法里有沉淀法和喷雾干燥法等方 法,固相法里有机械化粉碎法等。制造出来的纳米粉末因材料构造的微小化(100 nm以下)和随之而来的表面积的增加, 能表现出在原有的材料中无法被观察到的 特异的电、 磁、 机械及触媒特性。 因此, 可以应用到磁性零部件、 传感器、 过 滤器、 触媒等的新一代功能性材料当中。 The nanopowder refers to ultrafine particles which are not in the size and shape of the particles and have an average particle diameter of 100 nm or less. The manufacturing method of the nano powder can be classified into a gas phase method, a liquid phase method, and a solid phase method. Representative manufacturing methods using the gas phase method include a gas evaporation/condensation method and a gas phase synthesis method, and a liquid phase method includes a precipitation method and a spray drying method. The method has a mechanized pulverization method in the solid phase method. The manufactured nanopowder exhibits specific electrical, magnetic, mechanical, and catalytic properties that cannot be observed in the original material due to the miniaturization of the material structure (below 100 nm) and the accompanying increase in surface area. Therefore, it can be applied to a new generation of functional materials such as magnetic components, sensors, filters, and catalysts.
现有技术中纳米粒子的制造方法有多种方法, 大体上可分为物理方法和化 学方法。 因为化学方法利用的是化学反应, 需要使用氧化剂 (oxidizer)和还 原剂 (redUCtant)。 因此由化学反应制造出的纳米粒子在诸多反应过程中, 会 存在残留离子, 所以容易出现粒子之间的凝聚。 为了防止粒子间的凝聚, 通常 会使用表面活性剂(Surfactant)和分散剂(Dispersant)等添加剂, 所以纳米粒 子的纯度变的比较低。 制造应用产品时, 也容易与添加物产生反应, 在纳米粒 子制造流程结束后, 会产生有毒性的衍生物。 此外, 使用化学方式制造纳米粒 子的方法, 在混合惰性金属或相互不同性质的金属盐时, 很难制造出定量化的 纳米粒子, 所以在纳米粒子的材料选择上有着局限性。 由于存在此类问题, 使 用化学方式制造纳米粒子的方法会降低纳米粒子原有的功能, 需要对氧化剂、 还原剂、 残留酸等衍生物进行处理的额外费用。 There are various methods for fabricating nanoparticles in the prior art, which can be broadly classified into physical methods and chemical methods. Since the chemical method utilizes a chemical reaction, it is necessary to use an oxidizer and a reducing agent (red UC tant). Therefore, nanoparticles produced by chemical reactions may have residual ions in many reaction processes, so aggregation between particles is likely to occur. In order to prevent aggregation between particles, an additive such as a surfactant or a dispersant is usually used, so that the purity of the nanoparticles is relatively low. When the application product is manufactured, it is also easy to react with the additive, and after the completion of the nanoparticle production process, a toxic derivative is produced. In addition, the method of chemically manufacturing nanoparticles is difficult to produce quantitative nanoparticles when mixing inert metals or metal salts of different properties, so there are limitations in the material selection of the nanoparticles. Due to such problems, the method of chemically manufacturing nanoparticles reduces the original function of the nanoparticles, requiring additional costs for the treatment of oxidants, reducing agents, residual acids and the like.
用物理方法制造纳米粒子的方法可分为下向式(Top Down)方法和上向式 (Bottom Up)方法。下向式方法例如是把块状物用机械方法粉碎制造出纳米粒子; 上向式方法例如是指在材料中外加能源, 用蒸发 /凝缩的方法制造纳米粒子。 下 向式物理方式制造纳米粒子的代表例为机械式高能源粉碎法 (High Energy Mi lling),上向式的代表例为气相蒸发凝缩法(Inert Gas Condensation, IGC)。 上向式纳米粒子制造方法除了气相凝缩之外, 还有热蒸发(Thermal Evaporation)、 电子束蒸发 (E-beam Evaporation)、直流濺射 (DC Sputtering, DCS) , 射频溅射 (RF Sputtering, RFS)、 离子束溅射 (Ion Beam Sputtering, IBS) , 分子束外延 (Molecular Beam Epitaxy , MBE)、 火焰喷雾器进程(FAP, Flame Aerosol Process)、 化学气相沉禾只 (Chemical Vapor Deposition, CVD)、 化学气相合成 (Chemical Vapor Synthesis, CVS)、 电弧放电法(Arc Discharge Process)以及激光烧蚀 (Laser Ablation) 等多种方法。 现有的物理方式制造 纳米粉末的方法中普遍存在着如下问题: 粒子大小不均匀、 粒子大小难于控制、 制造工序效率低下并易产生污染以及大批量生产受局限等。 现有的物理方式制 造纳米粒子的方法中, 最具代表性的方法可分为机械粉碎法、 电爆破法、 惰性 气体凝缩法 (Inert Gas Condensation, IGC)等。 The method of physically manufacturing nanoparticles can be divided into a Top Down method and a Bottom Up method. The down-direct method is, for example, mechanically pulverizing the mass to produce nanoparticles; the upward-oriented method, for example, refers to the application of an energy source to the material to produce nanoparticles by evaporation/condensation. A representative example of a low-level physical manufacturing method of nanoparticles is a high-energy pulverization method (High Energy Mi lling), and an example of an upward-oriented method is an inert gas condensation (IGC). In addition to gas phase condensation, the upward-oriented nanoparticle production method includes thermal evaporation, E-beam evaporation, DC sputtering, DC sputtering, and RF sputtering. RFS), Ion Beam Sputtering (IBS), Molecular Beam Epitaxy (MBE), Flame Aerosol Process (FAP), Chemical Vapor Deposition (CVD), Chemical Vapor Synthesis (CVS), Arc Discharge (Arc Discharge) Process) and laser ablation (Laser Ablation) and other methods. The existing physical methods for manufacturing nanopowders generally have the following problems: uneven particle size, difficulty in controlling particle size, inefficient manufacturing processes, contamination, and limitations in mass production. Among the existing methods for physically manufacturing nanoparticles, the most representative methods can be classified into mechanical pulverization, electric blasting, and Inert Gas Condensation (IGC).
机械粉碎法虽然适合用在大批量生产上, 但是很难把纳米粒子的大小控制 在 lOOnm以下, 还有在粉碎过程中会出现污染的问题。  Although the mechanical pulverization method is suitable for mass production, it is difficult to control the size of the nanoparticles below 100 nm, and there is a problem of contamination during the pulverization process.
使用电爆破法制造纳米粒子的方法是,在真空内利用脉冲功率 (pulse power) 在蓄电池 (capacitor)的金属导线上, 瞬间释放已充电的高电压、 高电流来蒸发 /凝缩来制造纳米粒子。 由于此方法利用的是瞬间爆破, 所以存在难以控制纳米 粒子大小和需要重新收集纳米粒子后才能用的缺点。 虽然有人尝试在溶液内用 同一方法来制造纳米粒子, 但是此类方法也需分离溶液和纳米粉末之后才能使 用, 所以很难对工序进行单一化, 并获得纯纳米粒子。  The method of fabricating nanoparticles by electric blasting is to use a pulse power in a vacuum to produce a nanoparticle by instantaneously releasing a charged high voltage and a high current to evaporate/condense on a metal wire of a capacitor. . Since this method utilizes instantaneous blasting, there are disadvantages in that it is difficult to control the size of the nanoparticles and it is necessary to recollect the nanoparticles. Although some attempts have been made to produce nanoparticles by the same method in solution, such methods also require separation of the solution and the nanopowder, so that it is difficult to singulate the process and obtain pure nanoparticles.
惰性气体凝缩法虽然能制造出较高纯度的纳米粉末, 但是能用于制造的材 料有着局限性。 惰性气体凝缩法需要将纳米粒子凝缩在冷却棒之后, 需要重新 收集已凝缩的纳米粒子。 如要应用到最终产品, 需要经过附加工序处理, 所以 并不适于大批量生产。 由惰性气体凝缩法来制造出的纳米粉末, 由于会在大气 中急速氧化, 所以在真空槽内回收之后, 或者即刻应用到产品, 或者在真空槽 内注入少量的氧气, 缓慢氧化纳米粉末的表面来便于在空气中取送纳米粉末。 此类方法大部分在制造纳米粉末时, 不采用直接使用于应用产品中的支持体。 采用支持体来制造的纳米粉末[111], 容易取送, 使用最终产品的构成材料作为支 持体时, 可简单化制造工序。 但已有的专利或论文中提示到的纳米粉末制造装 置, 都存在着沉积效率低, 纳米粒子大小分布较宽, 支持体搅拌不均, 加载在 支持体上的负荷过重, 设备的耐用性低等问题。 特别在制造大批量生产用纳米 粒子制造装置时,存在着非效率性的连续沉积 (Deposition),支持体搅拌不均、 设备的耐用性低、 搅拌构造物的超负荷、 因支持体之间的负荷而引起的支持体 粉碎等问题。 Although the inert gas condensation method can produce a nanopowder of higher purity, the materials that can be used for manufacturing have limitations. The inert gas condensation process requires the nanoparticles to be condensed after the cooling rods, and the condensed nanoparticles need to be recollected. If it is to be applied to the final product, it needs to be processed through additional processes, so it is not suitable for mass production. The nanopowder produced by the inert gas condensation method is rapidly oxidized in the atmosphere, so it can be applied to the product immediately after being recovered in a vacuum chamber, or a small amount of oxygen is injected into the vacuum chamber to slowly oxidize the nanopowder. The surface facilitates the removal of nanopowder in air. Most of these methods do not use supports that are directly used in the application when manufacturing nanopowders. The nanopowder [ 1-11] manufactured by the support is easy to take, and when the constituent material of the final product is used as the support, the manufacturing process can be simplified. However, the nano-powder manufacturing devices suggested in the existing patents or papers have low deposition efficiency, wide nano-particle size distribution, uneven support agitation, excessive load on the support, and durability of the device. Low question. In particular, when manufacturing a nanoparticle production apparatus for mass production, there is inefficient continuous deposition, and the support is unevenly stirred. The durability of the equipment is low, the overload of the agitating structure, and the pulverization of the support due to the load between the supports.
连续沉积的情况是, 粒子会形成核并且核会成长, 核成长到与邻接的核产 生重叠的话, 纳米大小的粒子会急速成长为薄膜。 利用支持体制造大小均匀、 稳定的纳米粉末, 重要的是非连续性沉积, 即控制纳米材料沉积在支持体上的 时间和非沉积时间。 通过适当控制沉积时间来防止纳米粒子的过度成长, 在非 沉积时间, 使纳米粒子趋于稳定, 即使暴露在沉积区域, 纳米粒子也不会继续 成长, 在支持体上面形成别的核。 另外, 要制造纯净和均匀大小的纳米粒子, 必须要对支持体进行均匀搅拌。  In the case of continuous deposition, particles will form nuclei and the nuclei will grow. When the nuclei grow to overlap with adjacent nuclei, nanosized particles will rapidly grow into thin films. The use of a support to produce a uniform and stable nanopowder is important for discontinuous deposition, i.e., controlling the time and non-deposition time of nanomaterial deposition on the support. By appropriately controlling the deposition time to prevent excessive growth of the nanoparticles, the nanoparticles tend to be stable during the non-deposition time, and even if exposed to the deposition area, the nanoparticles do not continue to grow, forming other nuclei on the support. In addition, to produce pure and uniform size nanoparticles, the support must be uniformly agitated.
现在, 已经在产业领域当中使用多种沉积源 (例如利用电阻加热、 诱导加 热、 等离子射流 (Plasma Jet)、 电子束、 激光束的沉积源和利用离子束溅射、 DC (Direct Current)溅射、 RF (Radio Frequency)溅射、 电子回旋共振 (ECR, Electron Cyclotron Resonance)等的沉积源) 应用到纳米粒子制造装置中, 将 金属、 陶瓷、 氧化物、 有机物等多种材料制造成纳米粒子。  Now, various deposition sources have been used in the industrial field (for example, using resistance heating, induced heating, plasma jet, electron beam, laser beam deposition source, and ion beam sputtering, DC (Direct Current) sputtering. A deposition source such as RF (Radio Frequency) sputtering or Electron Cyclotron Resonance (ECR) is applied to a nanoparticle production apparatus to produce a variety of materials such as metals, ceramics, oxides, and organic materials into nanoparticles.
在先原有的物理方式的纳米粒子制造装置大部分都是以研究目的而制作的 案例, 其设计只适合用于少量生产, 此类装置并不适合产业化的大批量生产用。 以支持体搅拌方式制造纳米粒子的在先技术的例子见图 1-图 4。  Most of the original physical nanoparticle manufacturing devices were made for research purposes, and their design is only suitable for small-scale production. Such devices are not suitable for industrial mass production. A prior art example of manufacturing nanoparticles by support agitation is shown in Figures 1 - 4.
先前利用支持体制造纳米粉末或芯片的纳米粒子制造装置, 大部分都采用 水平搅拌轴搅拌的方式。 其中分为有采用单搅拌轴的和采用多个搅拌轴的情况。 图 1、 图 2所示的是水平轴搅拌方式的搅拌装置的例子。 这些装置由于搅拌槽 130, 230 的旋转, 支持体材料会向一个方向靠拢, 因而无法均匀搅拌支持体材 料。 图 1所示的搅拌装置是搅拌槽 130本体旋转的构造, 采取了圆桶型的水平 轴旋转方式的搅拌构造, 沉积源 111位于旋转桶内部。 图 1中采用向一个方向 131旋转圆桶的方式, 在搅拌过程中无法完全搅拌支持体 120, 旋转圆桶和支持 体材料相互滑动, 一些粉末有可能搅拌不到。 特别是存在凝聚力的支持体和搅 拌槽之间的滑落现象会更为严重。 为了解决这些问题, 需要对旋转圆桶构造进 行改进, 此外还有一个问题是沉积源位于旋转圆桶内部, 所以如果使用细小或 密度低的支持体材料的情况下, 沉积源被污染的可能性极高。 图 2显示了搅拌 装置中水平轴旋转方式的搅拌构造, 搅拌槽 230是固定的, 沉积源 211位于搅 拌槽外部。 图 2也同图 1中的装置一样, 由于旋转会出现支持体 220偏向一边 倾倒的现象, 并导致在特定领域中支持体材料过度堆积现象的产生, 因此很难 实现支持体材料的均匀搅拌。 此外, 在搅拌支持体材料时, 旋转翼 (或称搅拌 翼) 231暴露在上部, 至此纳米粒子沉积在旋转翼上, 像这样纳米粒子在不必要 的地方沉积的话, 会降低纳米粒子的沉积效率, 从而成为非效率性的工序。 用 单旋转轴构造来制造大批量生产装置, 有一定的局限性, 为了扩大容量, 在图 2 中可以使用多个单水平轴用串联来构成。 像这样设置多个轴的旋转轴的情况下, 各个旋转轴会向一定方向来旋转, 支持体材料会向同一方向移动, 使之不能实 现无法均匀搅拌的效果。 为了防止这种现象, 要需将旋转轴的旋转方向转换成 随机旋转。 搅拌轴的随机旋转会引起支持体材料之间的摩擦, 由旋转轴方向的 瞬间性旋转切换而造成支持体材料的无规律移动、 支持体搅拌不均匀、 支持体 材料的脱落、 设备的耐用性降低等诸多问题。 利用支持体材料制造纳米粒子的 方式中, 支持体材料的持续运动和均匀搅拌是比较重要的。 急速变化的旋转方 向会导致搅拌构造物对支持体材料加力, 造成支持体粒子严重粉碎或支持体材 料被瞬间風到外部的现象。 此外, 这些装置的缺点是随机搅拌将会发生热量, 所以不能使用不耐热的支持体材料。 支持体材料的粉碎会形成微小粒子, 从而 产生粉尘。 支持体从搅拌槽風出后流入到真空排气管里的话, 支持体材料会污 染真空泵, 缩短维修 /保养期限, 产生额外的维修 /保养费用, 并且降低产品的 生产效率。 此外, 急速变化的旋转方向切换, 会对旋转部位施加强大的外力, 降低设备的耐用性。 从纳米粒子的大小、 含量、 分布等控制性层来看, 如果无 法对支持体材料进行稳定和均匀搅拌, 则很难制造出一定大小的纳米粒子。 从 整体来看, 形成的大部分纳米粒子的大小不一的可能性会比较高。 Most of the nanoparticle manufacturing apparatuses that previously used the support to manufacture nanopowders or chips have been stirred by a horizontal stirring shaft. It is divided into a case where a single agitating shaft is used and a plurality of agitating shafts are used. Fig. 1 and Fig. 2 show an example of a stirring device of a horizontal axis stirring method. Due to the rotation of the agitation tanks 130, 230, the support materials are brought together in one direction, so that the support material cannot be uniformly stirred. The agitating device shown in Fig. 1 has a structure in which the agitating tank 130 rotates in the main body, and adopts a drum-type horizontal axis rotating type stirring structure, and the deposition source 111 is located inside the rotating tub. In Fig. 1, the drum is rotated in one direction 131. The support body 120 cannot be completely stirred during the stirring process, and the rotating drum and the support material slide with each other, and some powders may not be stirred. In particular, the slippage between the cohesive support and the agitation tank is more serious. In order to solve these problems, it is necessary to construct the rotating drum. There is also a problem in that the deposition source is located inside the rotating drum, so if a small or low density support material is used, the deposition source is highly likely to be contaminated. Fig. 2 shows a stirring structure of a horizontal shaft rotating mode in the stirring device, the stirring tank 230 is fixed, and the deposition source 211 is located outside the stirring tank. Fig. 2 is also the same as the apparatus of Fig. 1. Since the rotation of the support body 220 is tilted sideways due to the rotation, and the occurrence of excessive accumulation of the support material in a specific field is caused, it is difficult to achieve uniform agitation of the support material. In addition, when the support material is stirred, the rotating wing (or agitating wing) 231 is exposed to the upper portion, and thus the nanoparticles are deposited on the rotating wing, so that the deposition of the nanoparticles in unnecessary places reduces the deposition efficiency of the nanoparticles. , thus becoming an inefficient process. The use of a single rotating shaft configuration to manufacture a mass production device has certain limitations. To expand the capacity, a plurality of single horizontal axes can be used in series in FIG. When the rotating shafts of the plurality of shafts are provided as described above, the respective rotating shafts are rotated in a certain direction, and the support material is moved in the same direction, so that the effect of being unable to uniformly stir can not be achieved. In order to prevent this, it is necessary to convert the rotation direction of the rotary shaft into a random rotation. The random rotation of the agitator shaft causes friction between the support materials, which is caused by the instantaneous rotation of the rotating shaft direction, resulting in irregular movement of the support material, uneven support agitation, loss of the support material, and durability of the device. Reduce and many other issues. In the manner in which the nanoparticles are fabricated using the support material, continuous movement and uniform agitation of the support material are important. The rapidly changing direction of rotation causes the agitating structure to force the support material, causing severe comminution of the support particles or the support material being instantaneously blown to the outside. In addition, the disadvantage of these devices is that heat is generated by random agitation, so that a heat-resistant support material cannot be used. The pulverization of the support material forms fine particles, thereby generating dust. When the support body flows out of the agitation tank and flows into the vacuum exhaust pipe, the support material will contaminate the vacuum pump, shorten the repair/maintenance period, generate additional repair/maintenance costs, and reduce the production efficiency of the product. In addition, the rapid change of the direction of rotation switches a strong external force on the rotating part, reducing the durability of the device. From the viewpoint of the control layer such as the size, content, and distribution of the nanoparticles, if the support material cannot be stably and uniformly stirred, it is difficult to produce nanoparticles of a certain size. On the whole, most of the nanoparticles formed are more likely to be of different sizes.
图 3、 4所示是摆脱了水平旋转轴构造来制造纳米粒子的搅拌装置的例子。 图 3所示的装置可以看作和图 1装置类似的搅拌方式, 不同点是搅拌槽 330的 旋转轴从水平上具有一定角度, 沉积源 311 从搅拌槽内部移动到了外部位置。 像图 3这样的装置很难确保沉积区域, 所以在沉积的效率性和大容量的设备制 作上存在问题。 图 1 装置中所提示到的问题点相同, 会发生支持体材料从壁面 滑落的现象, 特别是搅拌支持体之间有凝聚力的微小粉末时, 很难实现微小粉 末的均匀搅拌。 因此, 此类装置很难解决支持体粉末的均匀搅拌和确保沉积区 域问题, 因此降低纳米制造工序的效率, 同时在制造大批量生产装置上存在局 限性。 图 4是搅拌轴采用垂直搅拌构造的搅拌装置的示例。 此类装置在搅拌溶 液相态的材料时, 是非常有效的方法, 但是在搅拌一定大小的固体形态的粉末 或芯片之类材料时, 为了混合上下两部位置的支持体材料, 需要提高搅拌翼的 旋转速度或更改其构造。 而提高搅拌翼速度的话, 不仅无法达到上下两部材料 的混合效率, 相反旋转翼周边材料将受到外力有可能会被粉碎掉。 所以, 此类 构造可以看作为比支持体材料的搅拌装置更适合的粉碎装置。 发明内容 Figures 3 and 4 show an example of a stirring device that detaches the horizontal rotating shaft structure to produce nanoparticles. The apparatus shown in Fig. 3 can be regarded as a stirring mode similar to that of Fig. 1, except that the rotating shaft of the stirring tank 330 has an angle from the horizontal, and the deposition source 311 is moved from the inside of the stirring tank to the outer position. A device such as that of FIG. 3 has difficulty in securing a deposition area, so there is a problem in the efficiency of deposition and the fabrication of a large-capacity device. In Fig. 1, the problem indicated in the apparatus is the same, and the phenomenon that the support material slides off from the wall surface occurs, and particularly when the fine powder having cohesive force between the support bodies is stirred, it is difficult to achieve uniform stirring of the fine powder. Therefore, such a device is difficult to solve the uniform agitation of the support powder and to ensure the deposition area problem, thereby reducing the efficiency of the nanofabrication process, and at the same time having limitations in manufacturing a mass production device. Fig. 4 is an example of a stirring device in which a stirring shaft adopts a vertical stirring configuration. Such a device is a very effective method for agitating a solution phase material, but when stirring a solid powder or chip or the like in a solid form, in order to mix the support materials at the upper and lower positions, it is necessary to increase the stirring blade. The speed of rotation or change its construction. When the speed of the stirring wing is increased, not only the mixing efficiency of the upper and lower materials cannot be achieved, but the material surrounding the rotating wing may be crushed by external force. Therefore, such a configuration can be regarded as a pulverizing device which is more suitable as a stirring device than a support material. Summary of the invention
有鉴于现有纳米粒子制造装置存在的各自的缺陷, 本发明的目的之一在于 提供一种搅拌装置, 以使支持体或支持体芯片混合均匀, 并减少支持体或支 持体芯片之间的摩擦。  In view of the respective drawbacks of existing nanoparticle manufacturing apparatuses, it is an object of the present invention to provide a stirring apparatus for uniformly mixing a support or a support chip and reducing friction between a support or a support chip. .
本发明的另一目的在于提供一种纳米粉末制造装置, 以制造出大小均匀 的纳米粉末。  Another object of the present invention is to provide a nanopowder manufacturing apparatus for producing a nano powder having a uniform size.
相应地, 本发明还提供一种纳米粉末制造方法, 以制造出大小均匀的纳 米粉末。  Accordingly, the present invention also provides a method of producing a nanopowder to produce a nano powder of uniform size.
为了实现上述目的, 本发明实施例提供一种搅拌装置, 该搅拌装置包括: 搅拌槽, 用于容纳纳米材料的支持体;  In order to achieve the above object, an embodiment of the present invention provides a stirring device, the stirring device comprising: a stirring tank for supporting a nano material;
垂直输送部件, 位于搅拌槽中, 用于通过螺旋式旋转将所述支持体从搅拌 槽的下部垂直输送至搅拌槽的上部; 以及  a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
支持板, 位于搅拌槽中以及垂直输送部件的上部, 用于支持所述垂直输送 部件输送来的支持体, 所述支持板为中间高、 外周低的锥形或锥台形。 a support plate located in the agitation tank and at the upper portion of the vertical conveying member for supporting the vertical conveying A support body that is conveyed by the component, wherein the support plate has a tapered shape or a truncated cone shape with a middle height and a low outer circumference.
为了实现上述目的, 本发明实施例还提供一种纳米粉末制造装置, 该装置 包括:  In order to achieve the above object, an embodiment of the present invention further provides a nano powder manufacturing apparatus, the apparatus comprising:
搅拌槽, 用于容纳纳米材料的支持体;  a stirring tank for supporting the nano material;
垂直输送部件, 位于搅拌槽中, 用于通过螺旋式旋转将所述支持体从搅拌 槽的下部垂直输送至搅拌槽的上部;  a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
支持板, 位于搅拌槽中以及垂直输送部件的上部, 用于支持所述垂直输送 部件输送来的支持体, 所述支持板为中间高、 外周低的锥形或锥台形; 以及 沉积装置, 沉积装置包括沉积源, 该沉积源位于搅拌槽中以及支持板的上 方, 用于利用物理沉积方式向支持体沉积纳米粉末。  a support plate, located in the agitation tank and in an upper portion of the vertical conveying member, for supporting the support conveyed by the vertical conveying member, the support plate being a middle-high, low-cone-shaped cone or frustum shape; and a deposition device, deposition The apparatus includes a deposition source located in the agitation tank and above the support plate for depositing the nanopowder to the support by physical deposition.
为了实现上述目的, 本发明实施例还提供一种纳米粉末制造方法, 该方法 包括:  In order to achieve the above object, an embodiment of the present invention further provides a method for manufacturing a nano powder, the method comprising:
装入步骤, 用于将支持体装入搅拌槽以及进行沉积源材料安装, 所述搅拌 槽及沉积源设置于处于大气状态的真空槽中;  a loading step for loading the support into the agitation tank and performing deposition source material installation, wherein the agitation tank and the deposition source are disposed in a vacuum chamber in an atmospheric state;
抽真空步骤, 利用真空泵对所述真空槽进行排气, 以使所述真空槽达到预 定的真空;  a vacuuming step of venting the vacuum chamber with a vacuum pump to bring the vacuum chamber to a predetermined vacuum;
搅拌及沉积步骤, 利用螺旋型垂直输送支持体的搅拌方式搅拌所述支持体, 在搅拌的同时通过物理沉积方式向处于沉积区域的支持体沉积纳米粉末;  a stirring and deposition step, stirring the support body by means of stirring of a spiral vertical conveying support, and depositing a nano powder by a physical deposition method to a support in a deposition area while stirring;
纳米粉末获取步骤, 打破真空槽内的真空, 从所述搅拌槽获取附着在支持 体上的纳米粉末。 该附着在支持体上的纳米粉末可经过后续加工或直接应用到 应用产品中。  The nanopowder acquisition step breaks the vacuum in the vacuum chamber, and the nanopowder attached to the support is obtained from the agitation tank. The nanopowder attached to the support can be processed later or applied directly to the application product.
本发明实施例的纳米粒子制造设备采用了螺旋型垂直输送方式的支持体搅 拌装置, 实现机械化负荷的最小化、 用一定速度和方向来输送支持体, 从而实 现对支持体进行均匀搅拌、 提高了沉积效率、 从而制造出一定大小的纳米粒子 的同时, 实现了机械性负荷和设备的负荷的最小化, 增进了设备耐用性的纳米 粒子制造装置。 附图说明 The nanoparticle manufacturing device of the embodiment of the invention adopts a spiral vertical conveying type support body stirring device to minimize the mechanized load and transport the support body with a certain speed and direction, thereby achieving uniform stirring and improvement of the support body. The deposition efficiency, thereby producing a certain size of nanoparticles, while realizing the mechanical load and the load of the device are minimized, and the nanoparticle manufacturing device for improving the durability of the device is realized. DRAWINGS
此处所说明的附图用来提供对本发明的进一步理解, 构成本申请的一部分, 并不构成对本发明的限定。 在附图中:  The drawings described herein are provided to provide a further understanding of the invention, and are not intended to limit the invention. In the drawing:
图 1为现有技术中采用水平轴旋转方式的搅拌装置的示意图之一;  1 is a schematic view of a stirring device using a horizontal axis rotation method in the prior art;
图 2为现有技术中采用水平轴旋转方式的搅拌装置的示意图之二;  2 is a second schematic view of a stirring device using a horizontal axis rotation method in the prior art;
图 3为现有技术中采用倾斜轴旋转方式的搅拌装置的示意图;  3 is a schematic view of a stirring device using a tilting shaft rotation mode in the prior art;
图 4为现有技术中采用垂直旋转方式的搅拌装置的示意图;  4 is a schematic view of a stirring device using a vertical rotation mode in the prior art;
图 5为本发明实施例中采用垂直输送方式的纳米粉末制造装置的结构示意 图;  5 is a schematic structural view of a nanopowder manufacturing apparatus adopting a vertical conveying method according to an embodiment of the present invention;
图 6为本发明实施例中上部支持体支持板及散播机的示意图;  6 is a schematic view of an upper support support plate and a spreader according to an embodiment of the present invention;
图 7为本发明实施例中纳米粉末制造装置的结构的简单示例;  7 is a simplified example of the structure of a nanopowder manufacturing apparatus in an embodiment of the present invention;
图 8为利用现有的纳米粉末制造装置制造出的银纳米粒子透射电子显微镜 (TEM) 图像示例;  8 is an example of a transmission electron microscope (TEM) image of a silver nanoparticle manufactured by using an existing nano powder manufacturing apparatus;
图 9根据本发明的纳米粉末制造装置制备出的银纳米粒子的 TEM图像示例; 图 10a与图 10b为根据本发明的纳米粉末制造装置制备出的银纳米粒子的大 小分布示意图。 具体实施方式  Fig. 9 is a TEM image example of silver nanoparticles prepared by the nanopowder manufacturing apparatus of the present invention; Figs. 10a and 10b are schematic diagrams showing the distribution of silver nanoparticles prepared by the nanopowder manufacturing apparatus according to the present invention. detailed description
为使本发明的目的、 技术方案和优点更加清楚, 下面结合附图对本发明的 具体实施例进行详细说明。 在此, 本发明的示意性实施例及其说明用于解释本 发明, 但并不作为对本发明的限定。  In order to make the objects, technical solutions and advantages of the present invention more comprehensible, the specific embodiments of the present invention will be described in detail below. The illustrative embodiments of the present invention and the description thereof are intended to be illustrative of the invention, but are not intended to limit the invention.
实施例一  Embodiment 1
本发明实施例提供一种用于纳米粉末制造的支持体搅拌装置及纳米粉末制 造装置。 图 5为本发明实施例中采用垂直输送方式的纳米粉末制造装置的结构示 意图, 图 7为更具体的示例图。 请参考图 5及图 7, 本实施例的纳米粉末制造装置 包括:  Embodiments of the present invention provide a support stirring device and a nano powder manufacturing device for nano powder manufacturing. Fig. 5 is a schematic view showing the structure of a nanopowder manufacturing apparatus adopting a vertical conveying method in the embodiment of the present invention, and Fig. 7 is a more specific example. Referring to FIG. 5 and FIG. 7, the nano powder manufacturing apparatus of this embodiment includes:
支持体搅拌装置, 该搅拌装置包括: 搅拌槽, 垂直输送部件, 支持板 534, 以及一个或一个以上的上部旋转翼 (或称散播机) 532; a support agitating device comprising: a stirring tank, a vertical conveying member, a support plate 534, And one or more upper rotors (or spreaders) 532;
沉积装置, 该沉积装置包括沉积源, 该沉积源位于搅拌装置的支持板的上 方, 用于利用物理沉积方式向支持体沉积纳米粉末;  a deposition device comprising a deposition source located above a support plate of the agitation device for depositing a nanopowder to the support by physical deposition;
真空槽, 容纳所述沉积源及搅拌装置, 该真空槽内保持真空状态, 以使所 述沉积源及搅拌装置处于真空中; 以及  a vacuum chamber for accommodating the deposition source and the stirring device, wherein the vacuum chamber is maintained in a vacuum state so that the deposition source and the stirring device are in a vacuum;
真空泵, 连接所述的真空槽, 用于对所述真空槽进行抽真空操作, 以保持 所述真空槽内的真空度。 本发明实施例中, 真空槽内真空度可根据需要控制在 5 X 10— 1 托至 1 X 10—6 托, 但并不限于此。 为了去除支持体所含水分、 气体或 挥发性物质, 可在所述搅拌槽外部设置加热装置 536, 以对搅拌槽内的支持体进 行加热。 而在真空槽内使用有挥发性支持体的情况下, 可在所述搅拌槽外部设 置冷却装置 536, 以对搅拌槽内的支持体进行冷却。 也可同时设置有加热及冷却 装置, 以根据需要决定是否开启所述加热或冷却装置。 A vacuum pump is connected to the vacuum chamber for vacuuming the vacuum chamber to maintain a vacuum in the vacuum chamber. In the embodiment of the present invention, the vacuum degree in the vacuum chamber can be controlled at 5 X 10 -1 Torr to 1 X 10 -6 Torr as needed, but is not limited thereto. In order to remove moisture, gas or volatile substances from the support, a heating device 536 may be provided outside the agitation tank to heat the support in the agitation tank. When a volatile support is used in the vacuum chamber, a cooling device 536 may be provided outside the agitation tank to cool the support in the agitation tank. It is also possible to provide heating and cooling means at the same time to decide whether to open the heating or cooling device as needed.
上述搅拌装置中:  In the above stirring device:
所述垂直输送部件位于搅拌槽 530中, 用于将所述支持体 520从搅拌槽的下 部垂直输送至搅拌槽的上部; 本实施例中, 所述垂直输送部件又包括: 旋转轴 及固定于该旋转轴上的螺旋形旋转翼。 为了描述方便, 也可称该垂直输送部件 为螺旋形主旋转轴 531或者螺旋形螺栓。  The vertical conveying member is located in the agitation tank 530 for vertically conveying the support body 520 from the lower portion of the agitation tank to the upper portion of the agitation tank. In this embodiment, the vertical conveying member further includes: a rotating shaft and a fixed A spiral rotor on the rotating shaft. For convenience of description, the vertical conveying member may also be referred to as a spiral main rotating shaft 531 or a spiral bolt.
所述支持板 534位于垂直输送部件的上部, 用于支持所述垂直输送部件输送 来的支持体, 为了有助于支持体在支持板上的滑动, 该支持板优选地设置为中 间 (接近旋转轴) 高、 外周 (远离旋转轴) 低的锥形或锥台形。 可选的, 所述 螺旋形主旋转轴 531的外周可设置一隔离筒, 筒的上部可与支持板设置为一体或 固定在一起, 筒的下部与搅拌槽的底部之间有一定空隙, 以使支持体通过该空 隙移动到主旋转轴, 并通过螺旋形旋转翼的旋转, 使支持体再次移动到搅拌槽 的上部。 当然, 该隔离筒的长度也可以设置得更短, 如仅围住螺旋形主旋转轴 的上部, 而露出下面的部分。 所述支持板与隔离筒可通过多种现有的方式 (如 通过支架等) 固定在搅拌槽中, 在此不进行详述。 所述一个或一个以上的上部旋转翼 (或称散播机) 532位于所述支持板上, 用 于搅拌所述支持板上的支持体。 The support plate 534 is located at an upper portion of the vertical conveying member for supporting the support body conveyed by the vertical conveying member, and the support plate is preferably disposed in the middle (close to rotation) in order to facilitate the sliding of the support body on the support plate. Axis) High, peripheral (away from the axis of rotation) Low cone or frustum shape. Optionally, an outer circumference of the spiral main rotating shaft 531 may be provided with a separating cylinder, and an upper portion of the cylinder may be integrally or fixedly connected with the supporting plate, and a gap between the lower portion of the cylinder and the bottom of the stirring tank may be The support is moved to the main rotation shaft through the gap, and the support is moved to the upper portion of the agitation tank by the rotation of the spiral rotor. Of course, the length of the spacer cylinder can also be set shorter, such as only enclosing the upper portion of the spiral main rotating shaft to expose the lower portion. The support plate and the isolation tube can be fixed in the agitation tank by various existing methods (such as by a bracket or the like), and will not be described in detail herein. The one or more upper rotors (or spreaders) 532 are located on the support plate for agitating the support on the support plate.
支持板上的支持体移动至支持板边缘并落下时掉落到所述搅拌槽中。  The support on the support plate is moved to the edge of the support plate and dropped into the agitation tank when it is dropped.
由于主旋转轴 531 的旋转是按一定方向来旋转, 不仅最小化了对支持体材 料的外加力, 也最小化了支持体粉末粉碎的现象, 以螺旋型螺栓 531 的旋转将 支持体材料移动到上部, 移动到上部的支持体材料随支持体支持板 534 的倾斜 面来移动的过程中同时经过沉积区域。 安装到沉积源的沉积材料可以使用像金、 银、 白金、 钌、 铑、 钯、 锇、 铱等贵金属或氧化物、 有机物、 合金、 普通金 属 (如铝 A1 ) 、 铯 (Se) 、 硅 (Si) 、 锗 (Ge)等材料作为沉积源的沉积材料。 在沉积材料具有导电性的情况下, 可使用 DC溅射、 离子束溅射等方法, 在沉积 材料不具有导电性的情况下, 可采用 RF溅射、 离子束溅射等方法, 但并不限于 此, 还可以采用中频溅射、 微波沉积、 双磁溅射、 热沉积、 电子束沉积、 激光 沉积、 电子回旋共振或离子镀等。 在沉积区域中, 由于上部搅拌翼 (散播机, spreader) 532的旋转带动, 支持体材料随支持板 534倾斜面来移动, 从而实现 均匀搅拌。 移动到支持板边缘位置的支持体会掉落到支持体搅拌槽中, 使沉积 到支持体上的纳米粒子获得到了稳定化的非沉积时间。 为了控制纳米粒子沉积 到支持体上的时间, 在支持板上钻一些孔 612 (如图 6所示) , 使支持体从支持 板上快速下落, 以此来控制支持体暴露时间, 从而控制沉积材料沉积到支持体 上的时间。 孔的数量和孔径的大小都可以进行变化。 在沉积区域中控制支持体 暴露时间实质上是指, 调节非沉积时间对比沉积时间的比率, 从而实现对支持 体表面纳米粒子大小的控制。 本发明中, 为了使支持体向下部顺畅地移动, 在 设计成搅拌槽 530 时, 设计成下部比上部窄小的构造 (即上粗下细) 。 为了均 匀搅拌下部的支持体还安装了至少一层下部旋转翼 533 (每一层与主旋转轴的角 度可不同, 并且每一层可设置两个或两个以上旋转翼) 。 所述上部旋转翼、 下 部旋转翼可固定于螺旋形主旋转轴 531上(但并不限于此) 。移动到搅拌槽 530 的支持体材料, 随着下部旋转翼 533连续的搅拌慢慢的移动到搅拌槽下部, 移 动到主旋转轴 531 的支持体通过螺栓的旋转, 再次移动到搅拌槽的上部。 反复 做此类过程, 由沉积源供应的纳米粒子会附着到粉末或芯片形态的支持体表面 上。 本发明的搅拌机结构是由螺旋型方式的支持体输送用主旋转轴、 上部搅拌 用辅助搅拌翼、 下部支持体搅拌用辅助搅拌翼等来构成的, 采用了垂直移送方 式的螺旋型旋转轴 531 来最大限度降低对支持体施加的外力。 另, 本实施例的 搅拌机在结构上, 为了在沉积区域中提高沉积效率, 还制作成了上部的支持体 搅拌部 532没有暴露在沉积源的结构, 即上部旋转翼埋在所述支持板上的支持 体中。 本发明实施例的具有如上搅拌机结构的纳米粒子制造装置在搅拌方式上 与现有的支持体搅拌方式相比, 具有能确保支持体材料的均匀搅拌性, 提高在 沉积区域中的沉积效率, 并在搅拌过程中最大程度上降低施加到支持体的外力 以来防止支持体粉碎等的长处。 本发明实施例的纳米粒子制造装置, 最大程度 上降低了真空泵的污染和搅拌轴的负荷, 并减少了设备的维修费用, 增进了设 备的耐用性。 依据本发明的纳米粒子制造装置在纳米粒子的控制上, 设计设备 时容易操作支持体体积对比沉积区域的表面积, 易于调节沉积时间对比非沉积 时间的比率调节, 总的来说易于调节纳米粒子的大小。 由本发明的纳米粉末制 造装置来制造出的纳米粉末平均大小可在 lnm-500nm范围之内, 沉积在支持体 上面的纳米粉末含量可在 lppm-10, OOOppm范围之内。 Since the rotation of the main rotating shaft 531 is rotated in a certain direction, not only the external force to the support material is minimized, but also the phenomenon that the support powder is pulverized is minimized, and the support material is moved to the rotation of the spiral bolt 531 to In the upper portion, the support material that moves to the upper portion passes through the deposition region while moving along the inclined surface of the support support plate 534. The deposition material to be deposited on the deposition source may use noble metals or oxides such as gold, silver, platinum, rhodium, ruthenium, palladium, iridium, osmium, etc., organic compounds, alloys, common metals (such as aluminum A1), bismuth (Se), silicon ( Materials such as Si) and germanium (Ge) are used as deposition materials for deposition sources. In the case where the deposition material is electrically conductive, methods such as DC sputtering and ion beam sputtering may be used. In the case where the deposition material does not have conductivity, RF sputtering, ion beam sputtering, or the like may be employed, but In this connection, intermediate frequency sputtering, microwave deposition, double magnetic sputtering, thermal deposition, electron beam deposition, laser deposition, electron cyclotron resonance or ion plating may also be employed. In the deposition area, due to the rotation of the upper agitating wing ( spreader) 532, the support material moves with the inclined surface of the support plate 534, thereby achieving uniform agitation. The support moved to the edge of the support plate is dropped into the support agitation tank to obtain a stabilized non-deposition time for the nanoparticles deposited on the support. In order to control the time during which the nanoparticles are deposited onto the support, holes 612 are drilled in the support plate (as shown in Figure 6) to allow the support to fall quickly from the support plate, thereby controlling the support exposure time and thereby controlling the deposition. The time the material is deposited onto the support. Both the number of holes and the size of the aperture can be varied. Controlling the support exposure time in the deposition zone essentially means adjusting the ratio of non-deposition time to deposition time to achieve control of the nanoparticle size of the support surface. In the present invention, in order to smoothly move the support body downward, when the stirring tank 530 is designed, the lower portion is made smaller than the upper portion (i.e., the upper portion is thicker and thinner). At least one lower rotating wing 533 is also installed in order to uniformly agitate the lower support (each layer may be different in angle from the main rotating shaft, and two or more rotating wings may be provided in each layer). The upper rotary wing and the lower rotary wing may be fixed to the spiral main rotation shaft 531 (but are not limited thereto). The support material moved to the agitation tank 530 is slowly moved to the lower part of the agitation tank as the lower rotary wing 533 is continuously stirred, and moved The support moved to the main rotating shaft 531 is moved to the upper portion of the stirring tank again by the rotation of the bolt. Repeatedly doing such a process, the nanoparticles supplied by the deposition source adhere to the surface of the support in the form of a powder or chip. The agitator structure of the present invention is constituted by a main-rotation shaft for conveying a support of a spiral type, an auxiliary agitating blade for upper agitation, an auxiliary agitating blade for agitating a lower support body, and the like, and a helical rotary shaft 531 adopting a vertical transfer method. To minimize the external force applied to the support. Further, in the structure of the agitator of the present embodiment, in order to improve the deposition efficiency in the deposition region, a structure in which the upper support agitating portion 532 is not exposed to the deposition source is formed, that is, the upper rotary wing is buried on the support plate. In the support body. The nanoparticle manufacturing apparatus having the above-described agitator structure according to the embodiment of the present invention has a uniform stirring property of the support material and a deposition efficiency in the deposition region, compared with the conventional support stirring method. The advantage of preventing the pulverization of the support or the like since the external force applied to the support is minimized during the stirring process. The nanoparticle manufacturing device of the embodiment of the invention minimizes the pollution of the vacuum pump and the load of the stirring shaft, reduces the maintenance cost of the equipment, and improves the durability of the equipment. The nanoparticle manufacturing apparatus according to the present invention can easily manipulate the surface area of the support volume when compared with the deposition area in the control of the nanoparticle, and can easily adjust the ratio of the deposition time to the non-deposition time, and is generally easy to adjust the nanoparticle. size. The nanopowders produced by the nanopowder manufacturing apparatus of the present invention may have an average size ranging from 1 nm to 500 nm, and the nanopowder deposited on the support may be in the range of 1 ppm to 10, OOO ppm.
本发明实施例的纳米粒子制造装置的工序流程分为选择纳米材料及支持体 材料、 装填纳米材料及支持体材料的装入阶段、 真空排气阶段、 纳米粉末制造 (搅拌 /沉积) 阶段、 打破真空阶段、 取出纳米粉末及支持体材料的阶段。 制造 纳米粉末, 首先要选择应用领域中适合的纳米目标材料和支持体材料。 作为纳 米粉末制造过程的前处理, 为了增进支持体和纳米粒子之间的粘贴力, 还可预 先在支持体表面采用现有技术常用的物理方法或化学方法进行预处理。 作为工 序准备, 在装入阶段, 选择了纳米材料和支持体材料之后, 在沉积源上安装纳 米材料锭块, 把支持体材料装入到搅拌槽中。 真空排气阶段, 在大气压状态下 利用低真空泵开始第 1 次真空排气, 达到适当的真空度之后, 利用高真空泵进 行第 2次真空排气。 在真空排气时, 为了有效的除去含在支持体材料上的空气 或支持体之间存在的空气, 可以利用搅拌机对装在搅拌槽内的支持体材料进行 搅拌。 此时为了更有效的除去真空槽内的空气, 可在搅拌槽的外部设置如图 5 所示的加热装置 (536)。 而在真空槽内使用有挥发性支持体的情况下, 可通过安 装冷却装置 (536)降低真空槽内的温度, 从而降低支持体挥的发程度。 完成真空 排气工程之后, 进入用沉积源在支持体上面成长纳米粒子的工序。 本工序中, 采用螺旋型垂直输送支持体的搅拌方式, 同时还可以对底部及上部支持体进行 辅助搅拌。 从沉积源供应的纳米材料在支持体材料上成长为纳米大小的粒子。 沉积 /搅拌工程阶段中,沉积在支持体上面的粒子暴露在沉积源时,粒子会成长, 达到一定大小的纳米粒子随支持体的搅拌从暴露在沉积领域向搅拌槽内部移 动。 移动到搅拌槽内部的纳米粒子, 再次随支持体暴露到沉积领域之前为止被 稳定, 会形成一定大小的纳米粒子。 如果纳米粒子稳定之前暴露到沉积区域的 话, 纳米粒子会更加成长, 很有可能成长为非常大的纳米粒子。 通过沉积时间 和非沉积时间的调节, 可以调节在支持体上面形成的纳米粒子大小。 在搅拌 /沉 积工序中, 可通过调节沉积率 ( Deposition Rate) 、 沉积时间、 沉积时间与非 沉积时间的比率 (与支持板的倾斜度、 支持板上孔的多少与大小等有关) 、 搅 拌速度、 蒸发源的温度、 支持体的温度、 真空度、 暴露在沉积区域下的全部支 持体表面积与该全部支持体体积的比等等条件来控制纳米粒子的大小和含量。 相对于现有的纳米粉末制造方法, 主要改进在于支持体的搅拌方式, 对于其他 的细节, 例如如何装入蒸发源、 如何蒸发、 如何抽真空等都是本技术领域的普 通技术人员可以完成的, 因此本发明省略对其详细的说明。 完成纳米粒子制造 工序之后, 作为最后阶段需打破真空槽内的真空, 从搅拌槽取出附着了纳米粉 末的支持体。 依据本发明的纳米粉末制造工序的又一长处是, 如果选择将最终 应用产品结构材料的材料作为支持体材料来使用的话, 可以简化工序, 而且因 为没有添加其他添加物, 所以它是亲环境的, 并可最大限度的发挥纳米粉末的 固有的特性。 图 8及图 9图示的分别是采用现有的水平旋转轴的纳米粉末制造装置及本 发明的具有垂直移送旋转轴的纳米粉末制造装置来制作出的银纳米粉末的透射 电子显微镜 (TEM) 图像示例。 由图 8及图 9明显可见, 利用本发明的纳米粒子 制造装置制造出的纳米粒子分布更加均匀。 The process flow of the nanoparticle manufacturing apparatus of the embodiment of the invention is divided into selecting a nano material and a support material, loading a nano material and a support material in a loading stage, a vacuum exhaust stage, a nano powder manufacturing (stirring/depositing) stage, and breaking The vacuum stage, the stage of taking out the nanopowder and the support material. To make nano-powders, first select the appropriate nano-target materials and support materials in the application field. As a pretreatment of the nanopowder manufacturing process, in order to enhance the adhesion between the support and the nanoparticles, the surface of the support may be pretreated in advance using physical or chemical methods commonly used in the prior art. As a process preparation, after the nano material and the support material are selected in the loading stage, the nano material ingot is mounted on the deposition source, and the support material is charged into the stirring tank. In the vacuum exhaust stage, the first vacuum is started by the low vacuum pump under atmospheric pressure, and after the appropriate vacuum is reached, the high vacuum pump is used. The second vacuum is exhausted. In order to effectively remove the air present between the air or the support contained in the support material during vacuum evacuation, the support material contained in the agitation tank may be stirred by a stirrer. At this time, in order to more effectively remove the air in the vacuum chamber, a heating device (536) as shown in Fig. 5 may be provided outside the stirring tank. In the case where a volatile support is used in the vacuum chamber, the temperature in the vacuum chamber can be lowered by installing a cooling device (536), thereby reducing the degree of support. After the vacuum evacuation process is completed, a process of growing nanoparticles on the support by the deposition source is entered. In this step, the stirring method of the spiral type vertical conveying support body is adopted, and the bottom and upper support bodies can also be assistedly stirred. The nanomaterial supplied from the deposition source grows on the support material into nanometer-sized particles. During the deposition/stirring stage, when the particles deposited on the support are exposed to the deposition source, the particles will grow, and the nanoparticles of a certain size will move from the exposed field to the inside of the stirred tank with the stirring of the support. The nanoparticles moving into the inside of the agitation tank are stabilized again before the support is exposed to the deposition field, and a certain size of nanoparticles is formed. If the nanoparticles are exposed to the deposition area before stabilization, the nanoparticles will grow more and are likely to grow into very large nanoparticles. The size of the nanoparticles formed on the support can be adjusted by adjustment of deposition time and non-deposition time. In the stirring/deposition process, the ratio of the deposition rate (Deposition Rate), the deposition time, the deposition time to the non-deposition time (related to the inclination of the support plate, the number and size of the holes on the support plate), and the stirring speed can be adjusted. The size and content of the nanoparticles are controlled by conditions such as the temperature of the evaporation source, the temperature of the support, the degree of vacuum, the ratio of the total surface area of the support exposed to the deposition area to the volume of the total support, and the like. Compared with the existing nanopowder manufacturing method, the main improvement lies in the manner of stirring of the support. For other details, such as how to charge the evaporation source, how to evaporate, how to evacuate, etc., it can be done by those skilled in the art. Therefore, the detailed description thereof is omitted in the present invention. After the completion of the nanoparticle production process, as a final stage, the vacuum in the vacuum chamber is broken, and the support to which the nanopowder is attached is taken out from the stirring tank. A further advantage of the nanopowder manufacturing process according to the present invention is that if the material of the final application product structural material is selected for use as a support material, the process can be simplified, and since it is not added with other additives, it is environmentally friendly. , and can maximize the inherent properties of nanopowders. 8 and 9 are transmission electron microscopes (TEM) of silver nanopowders produced by a nanopowder manufacturing apparatus using a conventional horizontal rotating shaft and a nanopowder manufacturing apparatus having a vertical transfer rotating shaft of the present invention, respectively. Image example. As is apparent from Figs. 8 and 9, the distribution of the nanoparticles produced by the nanoparticle production apparatus of the present invention is more uniform.
图 10a及图 10b所示分别为采用现有的纳米粉末制造装置及本发明的制造 纳米粉末的装置所造出的纳米粉末的大小分布的示例。 图 10a中比较了 2-30 nm 的纳米粉末的大小分布, 图 10b中比较了 10 nm以上的纳米粉末的大小分布。 其中 A表示采用现有搅拌方式来制造出的银纳米粒子, B表示采用本发明的搅拌 方式制造出的银纳米粒子。 图 10a及图 10b是以数量最多的粒子大小为基准相 对变换之后的结果 (即两曲线的峰值被标准化 (normalized) ) 。 由图 10a及 图 10b所示, 由现有的搅拌方式制造出的纳米粉末, 能观察到因不均匀的搅拌 而产生的很多大粒子。 采用本发明中的搅拌方式来制造出的纳米粉末, 能观察 到大粒子数量相对较少。 因此, 采用垂直输送方式的搅拌机可实现均匀搅拌, 抑制了大纳米粒子的生成。  Fig. 10a and Fig. 10b show examples of the size distribution of the nanopowders produced by the conventional nanopowder manufacturing apparatus and the apparatus for producing nanopowder of the present invention, respectively. Figure 10a compares the size distribution of nanopowders at 2-30 nm, and Figure 10b compares the size distribution of nanopowders above 10 nm. Wherein A represents silver nanoparticles produced by a conventional stirring method, and B represents silver nanoparticles produced by the stirring method of the present invention. Figures 10a and 10b show the results of the relative transformations based on the largest number of particle sizes (i.e., the peaks of the two curves are normalized). As shown in Figs. 10a and 10b, many of the large particles produced by the uneven stirring can be observed in the nanopowder produced by the conventional stirring method. The nanopowder produced by the stirring method of the present invention can observe that the number of large particles is relatively small. Therefore, the mixer using the vertical conveying method can achieve uniform agitation and suppress the formation of large nanoparticles.
图 8至图 10a、图 10b仅以银纳米粉末为例说明了本发明制备出的纳米粉末, 但本发明并不限于此。 利用本发明的纳米粉末制造装置, 同样可以制备出其他 材料的纳米粉末, 如同样可以制备出银以外的其他金属 (如金、 白金、 钌、 铑、 钯、 锇及铱等) 、 氧化物、 有机物、 合金及半导体 (如 Se 、 Si 及 Ge等) 等 材料的纳米粉末。  8 to 10a and 10b illustrate the nanopowder prepared by the present invention by taking silver nanopowder as an example, but the present invention is not limited thereto. With the nanopowder manufacturing apparatus of the present invention, nano powders of other materials can also be prepared, and other metals (such as gold, platinum, rhodium, ruthenium, palladium, iridium, ruthenium, etc.) and oxides can be prepared as well. Nano-powders of materials such as organic compounds, alloys, and semiconductors (such as Se, Si, and Ge).
对于利用现有的搅拌方式制造出来的纳米粉末来说, 10 nm以下的纳米粒子 能占所有纳米粒子的 89. 9%, 10 nm以上的纳米粒子占所有纳米粒子的 10. 1%。 而对于根据本发明利用垂直输送方式制造出来的纳米粉末来说, 无论是金属还 是其他材料 (如氧化物、 有机物、 合金、 Se 、 Si 及 Ge等) 的纳米粉末, 通过 调节适当的实验条件, 都可以达到以下指标: 10 nm以下的纳米粒子占所有纳米 粒子的 90%至 96. 1%, 10 nm以上的纳米粒子占所有纳米粒子的 3. 9%至 10%。 并且, 通过调节前面提到的沉积时间、 沉积时间与非沉积时间的比率、 搅拌速 度等条件, 可以控制生产的纳米粉末符合预定的指标, 例如, 可以控制生产的 纳米粉末, 使 10 nm以下的纳米粒子占 91%、 93%、 或 96%等, 同时 /或者使 10 nm 以上的纳米粒子占所有纳米粒子的 5%、 6 %、 或 8 %等, 但并不限于此。 For the nano-powders produced by the existing agitation method, the nanoparticles below 10 nm can account for 89.9% of all the nanoparticles, and the nanoparticles above 10 nm account for 10.1% of all the nanoparticles. For the nano-powder produced by the vertical transport method according to the present invention, the nano-powder of metal or other materials (such as oxide, organic, alloy, Se, Si, Ge, etc.) can be adjusted by adjusting the appropriate experimental conditions. The following indicators can be achieved: Nanoparticles below 10 nm account for 90% to 96.1% of all nanoparticles, and nanoparticles above 10 nm account for 3.9% to 10% of all nanoparticles. And, by adjusting the aforementioned deposition time, the ratio of deposition time to non-deposition time, and the stirring speed Conditions such as degree, can control the production of nano-powder to meet the predetermined indicators, for example, can control the production of nano-powder, so that nanoparticles below 10 nm account for 91%, 93%, or 96%, etc., and / or more than 10 nm The nanoparticles account for 5%, 6%, or 8% of all the nanoparticles, but are not limited thereto.
本发明中的纳米粒子制造装置是采用了前面列举的物理沉积方法来蒸发纳 米粒子, 在作为支持体 (Supporter)的粉末 (Powder) 或芯片 (Chip)上沉积纳米 粒子的工序来形成。 本发明采用无连续性的沉积方法来控制纳米粒子的成长, 有效果性的控制大小和含量的大批量生产纳米粉末的装置。  The nanoparticle production apparatus of the present invention is formed by a process of depositing nanoparticles on a powder or a chip as a supporter by a physical deposition method as exemplified above. The invention adopts a continuous deposition method to control the growth of nanoparticles, and has an effective device for controlling the size and content of mass production of nano powder.
本发明是采用一种全新概念的, 通过高效率的支持体搅拌方式, 与现有的 支持体搅拌方式相比更为增进了沉积效率和耐用性的优秀纳米粉末制造装置。 本发明使用的纳米粒子制造方式属于在真空内形成纳米粒子的上向式物理方式 纳米粒子制造方法。 本发明的纳米粒子制造设备采用了螺旋型垂直输送方式的 支持体搅拌方式, 实现机械化负荷的最小化、 用一定速度和方向来输送支持体, 从而实现对支持体进行均匀搅拌、 提高了沉积效率、 从而制造出一定大小的纳 米粒子的同时, 实现了机械性负荷和设备的负荷的最小化, 增进了设备耐用性 的纳米粒子制造装置。  The present invention is an excellent nano-powder manufacturing apparatus which enhances deposition efficiency and durability by a highly efficient support body stirring method compared with the existing support body stirring method. The nanoparticle production method used in the present invention belongs to an upward physical physical method nanoparticle production method for forming nanoparticles in a vacuum. The nanoparticle manufacturing device of the invention adopts a spiral vertical conveying mode support body stirring mode to minimize the mechanized load and transport the support body with a certain speed and direction, thereby achieving uniform stirring of the support body and improving deposition efficiency. In order to manufacture a certain size of nanoparticles, a nanoparticle manufacturing apparatus that achieves mechanical load and equipment load minimization and improves equipment durability is realized.
本发明中纳米粒子制造装置的搅拌方式采用了把支持体粉末或芯片以垂直 方式输送的方式, 以最小化支持体之间或支持体芯片之间的摩擦, 使其均匀混 合, 增进制造纳米粒子的效率和纳米粒子制造设备的耐用性, 是适用于大批量 生产设备的相关发明。 本发明是在真空内搅拌支持体粉末或芯片的同时, 还包 括利用沉积装置把纳米材料以纳米粒子大小沉积在粉末或芯片上面的工序。  In the nanoparticle manufacturing apparatus of the present invention, the stirring method adopts a method of conveying the support powder or the chip in a vertical manner to minimize the friction between the support or the support chip, and uniformly mix the nano particles. Efficiency and durability of nanoparticle manufacturing equipment are related inventions suitable for mass production equipment. The present invention is a process of agitating a support powder or a chip in a vacuum while further including depositing a nanomaterial on a powder or a chip by a deposition device.
以上所述的具体实施例, 对本发明的目的、 技术方案和有益效果进行了进 一步详细说明, 所应理解的是, 以上所述仅为本发明的具体实施例而已, 并不 用于限定本发明的保护范围, 凡在本发明的精神和原则之内, 所做的任何修改、 等同替换、 改进等, 均应包含在本发明的保护范围之内。 [I] 公开号为 GB1537839的英国专利申请。 The above described specific embodiments of the present invention are further described in detail, and are intended to be illustrative of the embodiments of the present invention. The scope of the protection, any modifications, equivalents, improvements, etc., made within the spirit and scope of the invention are intended to be included within the scope of the invention. [I] British Patent Application Publication No. GB1537839.
[2] High dispersion platinum catalyst by RF sputtering, J. Catal. 83 (1983), p. 477.  [2] High dispersion platinum catalyst by RF sputtering, J. Catal. 83 (1983), p. 477.
[3] High-dispersion d.c. sputtered platinum-titania powder catalyst active in ethane hydrogenolysis, J. Phys. Chem. 93 (1989), p. 1510. [3] High-dispersion d.c. sputtered platinum-titania powder catalyst active in ethane hydrogenolysis, J. Phys. Chem. 93 (1989), p. 1510.
[4] Nanoparticles of gold on γ-Α1203 produced by dc magnetron sputtering, J. Catal. 231 (2005), p.151. [4] Nanoparticles of gold on γ-Α1203 produced by dc magnetron sputtering, J. Catal. 231 (2005), p.151.
[5] Gold catalysts prepared by coprecipitation for low-temperature oxidation of hydrogen and of carbon monoxide, J. Catal. 115 (1989), p. 301.  [5] Gold catalysts prepared by coprecipitation for low-temperature oxidation of hydrogen and of carbon monoxide, J. Catal. 115 (1989), p. 301.
[6] A technique for sputter coating of ceramic reinforcement particles, Surf. Coat. Technol. 91 (1997), p. 64.  [6] A technique for sputter coating of ceramic reinforcement particles, Surf. Coat. Technol. 91 (1997), p. 64.
[7] Catalysis by Gold, Catal. Rev.-Sci. Eng. 41 (1999), p. 319.  [7] Catalysis by Gold, Catal. Rev.-Sci. Eng. 41 (1999), p. 319.
[8] Gold: a relatively new catalyst, Catal. Today 72 (2002), p. 5. [8] Gold: a relatively new catalyst, Catal. Today 72 (2002), p. 5.
[9] Surface treatment of aluminum oxide and tungsten carbide powders by ion beam sputter deposition, Surf. Coat. Technol. 163-164 (2003), p. 281.  [9] Surface treatment of aluminum oxide and tungsten carbide powders by ion beam sputter deposition, Surf. Coat. Technol. 163-164 (2003), p. 281.
[10] Gold as a Novel Catalyst in the 21st Century: Preparation, Working Mechanisms and Applications, Gold Bull. 37 (2004), p. 27 [10] Gold as a Novel Catalyst in the 21st Century: Preparation, Working Mechanisms and Applications, Gold Bull. 37 (2004), p. 27
[I I] Oxidation of CO on Gold Supported Catalysts Prepared by Laser Vaporization: Direct Evidence of Support Contribution, J. Am. Chem. Soc. 126 (2004), p. 1199.  [I I] Oxidation of CO on Gold Supported Catalysts Prepared by Laser Vaporization: Direct Evidence of Support Contribution, J. Am. Chem. Soc. 126 (2004), p. 1199.
[12] 韩国专利申请 No.KR1005862700000。  [12] Korean Patent Application No. KR1005862700000.

Claims

1. 一种纳米粉末制造装置, 其特征在于, 该装置包括: A nano powder manufacturing apparatus, characterized in that the apparatus comprises:
搅拌槽, 用于容纳纳米材料的支持体;  a stirring tank for supporting the nano material;
垂直输送部件, 位于搅拌槽中, 用于通过螺旋式旋转将所述支持体从搅拌 槽的下部垂直输送至搅拌槽的上部;  a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
支持板, 位于搅拌槽中以及垂直输送部件的上部, 用于支持所述垂直输送 权  a support plate located in the agitation tank and at the upper portion of the vertical conveying member for supporting the vertical conveying right
部件输送来的支持体, 所述支持板为中间高、 外周低的锥形或锥台形; 以及 沉积装置, 沉积装置包括沉积源, 该沉积源位于搅拌槽中以及支持板的上 方, 用于利用物理沉积方式向支持体沉积纳米粉末。 a support body to which the component is conveyed, the support plate is a cone-shaped or frustum-shaped shape having a middle height and a low circumference; and a deposition device including a deposition source located in the agitation tank and above the support plate for utilizing The physical deposition method deposits a nanopowder onto the support.
2.根据权利要求 1所述的制造装置, 其特征求在于, 该制造装置还包括: 一个或一个以上的上部旋转翼, 位于所述支持板上, 用于搅拌所述支持板 上的支持体。  2. The manufacturing apparatus according to claim 1, wherein the manufacturing apparatus further comprises: one or more upper rotary blades on the support plate for agitating the support on the support plate .
3.根据权利要求 1所述的制造装置, 其特征在于, 该制造装置还包括: 一个或一个以上的下部旋转翼, 位于所述搅拌槽中, 用于对搅拌槽中的支 持体进行搅拌。  The manufacturing apparatus according to claim 1, further comprising: one or more lower rotary blades located in the agitation tank for agitating the support in the agitation tank.
4. 根据权利要求 2或 3所述的制造装置, 其特征在于: 所述垂直输送部件包括: 旋转轴及固定于该旋转轴上的螺旋形旋转翼。 The manufacturing apparatus according to claim 2 or 3, wherein the vertical conveying member comprises: a rotating shaft and a spiral rotating wing fixed to the rotating shaft.
5. 根据权利要求 4所述的制造装置, 其特征在于: 所述上部旋转翼、 下部旋转翼固定于所述旋转轴上。 The manufacturing apparatus according to claim 4, wherein the upper rotating wing and the lower rotating blade are fixed to the rotating shaft.
6. 根据权利要求 1所述的制造装置, 其特征在于:  6. The manufacturing apparatus according to claim 1, wherein:
所述上部旋转翼埋在所述支持板上的支持体中。  The upper rotating wing is embedded in a support on the support plate.
7. 根据权利要求 1所述的制造装置, 其特征在于:  7. The manufacturing apparatus according to claim 1, wherein:
所述支持板上设置有一个或一个以上的孔。  One or more holes are provided on the support plate.
8. 根据权利要求 1所述的制造装置, 其特征在于:  8. The manufacturing apparatus according to claim 1, wherein:
所述搅拌槽上粗下细。 The stirring tank is thick and thin.
9. 根据权利要求 1所述的制造装置, 其特征在于, 该制造装置还包括: 设置于所述搅拌槽外部的加热装置, 用于对搅拌槽内的支持体进行加热。9. The manufacturing apparatus according to claim 1, further comprising: a heating device provided outside the stirring tank for heating the support in the stirring tank.
10. 根据权利要求 1所述的制造装置, 其特征在于, 该制造装置还包括: 设置于所述搅拌槽外部的冷却装置, 用于对搅拌槽内的支持体进行冷却。10. The manufacturing apparatus according to claim 1, further comprising: a cooling device disposed outside the agitation tank for cooling the support in the agitation tank.
11. 根据权利要求 1所述的制造装置, 其特征在于, 该制造装置还包括: 真空槽, 设置于所述沉积源及搅拌槽的外部; 以及 11. The manufacturing apparatus according to claim 1, further comprising: a vacuum chamber disposed outside the deposition source and the agitation tank;
真空泵, 用于抽取真空槽内的气体, 以保持所述真空槽内部为真空状态。 A vacuum pump is used to extract the gas in the vacuum chamber to keep the inside of the vacuum chamber in a vacuum state.
12. 根据权利要求 1所述的纳米粉末制造装置, 其特征在于: 12. The nanopowder manufacturing apparatus according to claim 1, wherein:
所述沉积源的材料包括: 金属、 氧化物、 有机物、 合金及半导体中的至少 一种。  The material of the deposition source includes at least one of a metal, an oxide, an organic compound, an alloy, and a semiconductor.
13. 根据权利要求 12所述的纳米粉末制造装置, 其特征在于:  13. The nanopowder manufacturing apparatus according to claim 12, wherein:
所述金属为金、 银、 白金、 钌、 铑、 钯、 锇及铱。  The metals are gold, silver, platinum, rhodium, ruthenium, palladium, iridium and osmium.
14. 根据权利要求 1所述的纳米粉末制造装置, 其特征在于:  14. The nanopowder manufacturing apparatus according to claim 1, wherein:
所述物理沉积方式包括: 直流溅射、 射频溅射、 中频溅射、 离子束溅射、 微波沉积、 双磁溅射、 热沉积、 电子束沉积、 激光沉积或离子镀。  The physical deposition methods include: direct current sputtering, radio frequency sputtering, medium frequency sputtering, ion beam sputtering, microwave deposition, double magnetic sputtering, thermal deposition, electron beam deposition, laser deposition, or ion plating.
15.—种纳米粉末制造方法, 其特征在于, 该方法包括如下步骤:  15. A nano powder manufacturing method, characterized in that the method comprises the following steps:
装入步骤, 用于将支持体装入搅拌槽以及进行沉积源材料安装, 所述搅拌 槽及沉积源设置于处于大气状态的真空槽中;  a loading step for loading the support into the agitation tank and performing deposition source material installation, wherein the agitation tank and the deposition source are disposed in a vacuum chamber in an atmospheric state;
抽真空步骤, 利用真空泵对所述真空槽进行排气, 以使所述真空槽达到预 定的真空;  a vacuuming step of venting the vacuum chamber with a vacuum pump to bring the vacuum chamber to a predetermined vacuum;
搅拌及沉积步骤, 利用螺旋型垂直输送支持体的搅拌方式搅拌所述支持体, 在搅拌的同时通过物理沉积方式向处于沉积区域的支持体沉积纳米粉末;  a stirring and deposition step, stirring the support body by means of stirring of a spiral vertical conveying support, and depositing a nano powder by a physical deposition method to a support in a deposition area while stirring;
纳米粉末获取步骤, 破坏真空槽内的真空, 从所述搅拌槽中获取附着在支 持体上的纳米粉末。  The nanopowder acquisition step destroys the vacuum in the vacuum chamber, and the nanopowder attached to the support is obtained from the agitation tank.
16. 根据权利要求 15所述的方法, 其特征在于:  16. The method of claim 15 wherein:
所述抽真空步骤还包括利用螺旋型垂直输送支持体的搅拌方式搅拌所述支 持体。 The evacuating step further includes agitating the branch by a stirring method of a spiral vertical conveying support Hold the body.
17. 根据权利要求 15所述的方法, 其特征在于:  17. The method of claim 15 wherein:
所述搅拌及沉积步骤还包括对所述搅拌槽内的支持体进行冷却。  The agitation and deposition step further includes cooling the support in the agitation tank.
18. 根据权利要求 15所述的方法, 其特征在于:  18. The method of claim 15 wherein:
所述装入步骤之前还包括对所述支持体进行预处理。  The loading step also includes pre-treating the support prior to the loading step.
19. 根据权利要求 15所述的方法, 其特征在于:  19. The method of claim 15 wherein:
所述物理沉积方式包括: 直流溅射、 射频溅射、 中频溅射、 离子束溅射、 微波沉积、 双磁溅射、 热沉积、 电子束沉积、 激光沉积或离子镀。  The physical deposition methods include: direct current sputtering, radio frequency sputtering, medium frequency sputtering, ion beam sputtering, microwave deposition, double magnetic sputtering, thermal deposition, electron beam deposition, laser deposition, or ion plating.
20. 根据权利要求 15所述的方法, 其特征在于:  20. The method of claim 15 wherein:
所述沉积源材料包括: 金属、 氧化物、 有机物、 合金 或半导体。  The deposition source material includes: a metal, an oxide, an organic, an alloy, or a semiconductor.
21. 一种用于纳米粉末制造的搅拌装置, 其特征在于, 该装置包括: 搅拌槽, 用于容纳纳米材料的支持体;  21. A stirring device for nano powder manufacturing, characterized in that the device comprises: a stirring tank for supporting a nano material;
垂直输送部件, 位于搅拌槽中, 用于通过螺旋式旋转将所述支持体从搅拌 槽的下部垂直输送至搅拌槽的上部; 以及  a vertical conveying member located in the agitation tank for vertically conveying the support body from a lower portion of the agitation tank to an upper portion of the agitation tank by a spiral rotation;
支持板, 位于搅拌槽中以及垂直输送部件的上部, 用于支持所述垂直输送 部件输送来的支持体, 所述支持板为中间高、 外周低的锥形或锥台形。  The support plate is located in the agitation tank and in the upper portion of the vertical conveying member for supporting the support conveyed by the vertical conveying member, and the support plate has a tapered shape or a truncated cone shape which is high in the middle and low in the outer circumference.
22.根据权利要求 21所述的搅拌装置, 其特征在于, 该搅拌装置还包括: 一个或一个以上的上部旋转翼, 位于所述支持板上, 用于搅拌所述支持板 上的支持体。  22. The agitation device of claim 21, further comprising: one or more upper rotors on the support plate for agitating the support on the support plate.
23.根据权利要求 21所述的搅拌装置, 其特征在于, 该搅拌装置还包括: 一个或一个以上的下部旋转翼, 位于所述搅拌槽中, 用于对搅拌槽中的支 持体进行搅拌。  The agitation device according to claim 21, further comprising: one or more lower rotary blades located in the agitation tank for agitating the support in the agitation tank.
24. 根据权利要求 22或 23所述的搅拌装置, 其特征在于:  24. A stirring apparatus according to claim 22 or 23, wherein:
所述垂直输送部件包括: 旋转轴及固定于该旋转轴上的螺旋形旋转翼。 The vertical conveying member includes: a rotating shaft and a spiral rotating wing fixed to the rotating shaft.
25. 根据权利要求 24所述的搅拌装置, 其特征在于: 25. The agitation device of claim 24, wherein:
所述上部旋转翼、 下部旋转翼固定于所述旋转轴上。 The upper rotary wing and the lower rotary wing are fixed to the rotating shaft.
26. 根据权利要求 21所述的搅拌装置, 其特征在于: 26. The agitation device of claim 21, wherein:
所述上部旋转翼埋在所述支持板上的支持体中。  The upper rotating wing is embedded in a support on the support plate.
27. 根据权利要求 21所述的搅拌装置, 其特征在于:  27. The stirring apparatus according to claim 21, wherein:
所述支持板上设置有一个或一个以上的孔。  One or more holes are provided on the support plate.
28. 根据权利要求 21所述的搅拌装置, 其特征在于:  28. The stirring apparatus according to claim 21, wherein:
所述搅拌槽上粗下细。  The stirring tank is thick and thin.
29. 根据权利要求 21所述的搅拌装置, 其特征在于, 该搅拌装置还包括: 设置于所述搅拌槽外部的加热装置, 用于对搅拌槽内的支持体进行加热。 The agitation device according to claim 21, further comprising: a heating device disposed outside the agitation tank for heating the support in the agitation tank.
30. 根据权利要求 21所述的搅拌装置, 其特征在于, 该搅拌装置还包括: 设置于所述搅拌槽外部的冷却装置, 用于对搅拌槽内的支持体进行冷却。 30. The agitation device according to claim 21, further comprising: a cooling device disposed outside the agitation tank for cooling the support in the agitation tank.
PCT/CN2008/070675 2008-01-22 2008-04-03 A stirring device, a device with said stirring device for producing nanometer powder and its method WO2009092207A1 (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012016382A1 (en) * 2010-08-05 2012-02-09 大连科林爱纳米科技有限公司 Metal nanocatalyst and preparation method thereof
WO2019071282A1 (en) * 2017-10-03 2019-04-18 Goetschl Franz Mixing device and method for producing a fibre-reinforced concrete

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108237478A (en) * 2016-12-23 2018-07-03 浙江金徕镀膜有限公司 Polishing fluid stirs pumping all-in-one machine and polishing machine

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57127431A (en) * 1981-01-29 1982-08-07 Nitsukuu Kogyo Kk Vacuum mixing and defoaming machine
CN2098963U (en) * 1990-12-18 1992-03-18 肖彪 Multi-function fountain type mixer
CN2354647Y (en) * 1997-12-15 1999-12-22 南通罗斯混合设备有限公司 Vertical mixer
CN2403493Y (en) * 1999-07-12 2000-11-01 王华业 Spiral cone stirring homogenizer
CN1488462A (en) * 2003-08-20 2004-04-14 东华大学 Nano particle surface physicochemical structure cutting and coating method
CN1496756A (en) * 2002-09-25 2004-05-19 �仯��ҵ��ʽ���� Stirring mixer and stirring mixing method
CN1723294A (en) * 2002-12-25 2006-01-18 友技科株式会社 Polygonal barrel spattering device, polygonal barrel spattering method, coated particle formed by the device and method, microcapsule, and method of manufacturing the microcapsule
CN101073771A (en) * 2007-06-21 2007-11-21 浙江工业大学 Method for producing nano-carbon tube load platinum catalyst by laser deposition

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57127431A (en) * 1981-01-29 1982-08-07 Nitsukuu Kogyo Kk Vacuum mixing and defoaming machine
CN2098963U (en) * 1990-12-18 1992-03-18 肖彪 Multi-function fountain type mixer
CN2354647Y (en) * 1997-12-15 1999-12-22 南通罗斯混合设备有限公司 Vertical mixer
CN2403493Y (en) * 1999-07-12 2000-11-01 王华业 Spiral cone stirring homogenizer
CN1496756A (en) * 2002-09-25 2004-05-19 �仯��ҵ��ʽ���� Stirring mixer and stirring mixing method
CN1723294A (en) * 2002-12-25 2006-01-18 友技科株式会社 Polygonal barrel spattering device, polygonal barrel spattering method, coated particle formed by the device and method, microcapsule, and method of manufacturing the microcapsule
CN1488462A (en) * 2003-08-20 2004-04-14 东华大学 Nano particle surface physicochemical structure cutting and coating method
CN101073771A (en) * 2007-06-21 2007-11-21 浙江工业大学 Method for producing nano-carbon tube load platinum catalyst by laser deposition

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012016382A1 (en) * 2010-08-05 2012-02-09 大连科林爱纳米科技有限公司 Metal nanocatalyst and preparation method thereof
WO2019071282A1 (en) * 2017-10-03 2019-04-18 Goetschl Franz Mixing device and method for producing a fibre-reinforced concrete

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