1. Field of the Invention
The present invention relates to the synthesis of metal oxide nanopowders, and more specifically to a method of synthesizing metal oxide nanopowders by rapid microwave combustion.
2. Description of the Related Art
Nanoparticles, including nanopowders, nanoclusters and nanocrystals, are small particles that have at least one dimension less than 100 nm. Nanoparticle research is currently an intense area of scientific research due to a wide variety of potential applications in the biomedical, optical and electronic fields.
Nanoparticles are effectively a bridge between bulk materials and atomic or molecular structures. A bulk material should have constant physical properties regardless of its size, but at the nanoscale level this is often not the case. Size-dependent properties are observed, such as quantum confinement in semiconductor particles, surface plasmon resonance in some metal particles, and superparamagnetism in magnetic materials.
The properties of materials change as their size approaches the nanoscale and as the percentage of atoms at the surface of a material becomes significant. For bulk materials larger than one micrometer, the percentage of atoms at the surface is minuscule relative to the total number of atoms of the material. The interesting and sometimes unexpected properties of nanoparticles are partly due to the aspects of the surface of the material dominating the properties in lieu of the bulk properties.
There are several methods for creating nanoparticles. Attrition and pyrolysis are common methods. In attrition, macro- or microscale particles are ground in a ball mill, a planetary ball mill, or other size-reducing mechanism. The method is simple and inexpensive, but can produce a broad particle size distribution, and the milling tool can possibly introduce contamination into the nanopowder.
In pyrolysis, a liquid or gas organic precursor is forced through an orifice at high pressure and burned. The resulting ash is air classified to recover the metal oxide nanoparticles. In the liquid phase method, nanoparticles are produced from a mixture of chemicals that react when heated to a certain temperature. The liquid phase method is effective, but there are additional costs resulting from the use of solvents and the production of large amounts of wastewater.
Gas phase synthesis methods are used extensively in industry to produce nanopowder metal oxide. These methods usually use supersaturated gases that are unstable relative to the formation of the solid material in nanoparticulate form. These methods can be classified by the phase of the precursor and the energy source used. The precursor could be in the solid, liquid or vapor phase. Conventional heating, solar energy, and laser or electromagnetic radiation energy can usually achieve conversion of the phase of the precursor from solid or liquid to gas phase.
A thermal plasma can also deliver the energy necessary to cause evaporation of small micrometer-size particles. The thermal plasma temperatures are in the order of 10,000K, so that the solid powder easily evaporates. Nanoparticles are formed upon cooling while exiting the plasma region. The main types of thermal plasma torches used to produce nanoparticles are dc plasma jet, dc arc plasma, and radio frequency (RF) induction plasmas. In the arc plasma reactors, the energy necessary for evaporation and reaction is provided by an electric arc that forms between the anode and the cathode. In RF induction plasma torches, energy coupling to the plasma is accomplished through the electromagnetic field generated by the induction coil. The plasma gas does not come in contact with electrodes, thus eliminating possible sources of contamination and allowing the operation of such plasma torches with a wide range of gases, including inert, reducing, oxidizing and other corrosive atmospheres. The working frequency is typically between 200 kHz and 40 MHz. Laboratory units run at power levels in the order of 30-50 kW, while the large-scale industrial units have been tested at power levels up to 1 MW. The RF plasma method has been used to synthesize different nanoparticle materials, for example, synthesis of various ceramic nanoparticles, such as oxides, carbours/carbides, and nitrides of Ti and Si.
None of the above methods, taken either singly or in combination, is seen to describe the instant invention as claimed. Thus, a method for synthesizing metal oxide solving the aforementioned problems is desired.
The method for synthesizing metal oxide provides a method for producing metal oxide nanoparticles by subjecting low boiling point metals or a combination of low boiling point metals to microwave energy from a conventional 2.45 GHz microwave oven.
The microwave energy is transferred to the metal as heat through the use of a microwave susceptor. Inside the susceptor, the metal will absorb the heat and evaporate into small particles. The small particles then combust in air, forming nanosize powder.
Increasing the length of the susceptor tube and controlling the amount of metal inserted inside the tube can control the size of the nanoparticle. The method can also be used for doping the nanopowder with other metals, such as Ni, Cu, Al, Sn, Zn, In, Te and Bi.
The susceptor is an open-ended tube that is made of silicon carbide (SiC) composite material. The composite is very stable and will not chemically interact with the metal at the elevated temperatures produced inside the susceptor tube. The susceptor has microwave-transparent thermal shielding. The metal is placed into the susceptor tube and then placed inside a conventional microwave oven. This method can produce large quantities of nanopowder quickly and inexpensively.
These and other features of the present invention will become readily apparent upon further review of the following specification and drawings.
Similar reference characters denote corresponding features consistently throughout the attached drawings.
The present invention relates generally to the synthesis of metal oxide nanopowders, and more particularly to a method for synthesizing metal oxide nanopowders by rapid microwave combustion.
The temperature is monitored with a thermocouple 22, and the susceptor 18 is heated to a temperature above the boiling point of the subject metal, usually above 700° C. The subject metal (such as Zn, Bi, Te and Sr), which has a low boiling point, is placed into the susceptor tube 18 by passing the metal through a ceramic inlet tube 12. The metal boils on contact with the interior of the susceptor tube 18 and is converted into vapor. The high temperature vapor combusts with any residual air in the susceptor tube 18, forming a metal oxide vapor. A flow of nitrogen or argon 28 may be used to replace the residual air in the susceptor tube 18 to control the rate of combustion of the vapor.
As the metal boils in the susceptor tube 18, the resulting high temperature vapor rises and comes into contact with the residual air, or with oxygen brought into the susceptor tube 18 through a port 16 by a pump 26. The reaction of the metal with the oxygen produces metal oxide, which continues to rise in the susceptor tube 18. The vapor droplet size decreases as the vapor travels farther up the susceptor tube 18, resulting in smaller particles of nanopowder. Increasing the length of the susceptor tube 18 can control the size of the nanoparticles. The metal oxide vapor exits the tube 18 and condenses as nanopowder on the interior surface of the collecting device 14. Scanning electron microscopy (SEM) and x-ray diffraction (XRD) techniques may then characterize the nanopowder.
The method is further illustrated by the following example.
This example describes one process for producing ZnO nanopowder using the microwave rapid combustion method.
The susceptor tube was placed into the thermal shielding and placed in the interior of a conventional 1.5 kW microwave oven. The oven was started and the temperature of the susceptor tube was monitored with a thermocouple. After approximately four minutes, the temperature of the susceptor tube was 700° C. A 2-gram quantity of zinc (Zn) was inserted through the ceramic inlet tube. After 15 seconds, the Zn evaporated and interacted with the residual oxygen inside the susceptor tube. The resulting combustion formed zinc oxide (ZnO) vapor. The vapor exited from the susceptor tube and interacted with the air to condense as ZnO nanopowder. The nanopowder deposited on the interior surface of the collecting device, which, for this example, was an ordinary beaker. The nanopowder was collected and characterized.
It is to be understood that the present invention is not limited to the embodiment described above, but encompasses any and all embodiments within the scope of the following claims.
Number | Name | Date | Kind |
---|---|---|---|
4753675 | Ovshinsky et al. | Jun 1988 | A |
4943316 | Taylor | Jul 1990 | A |
5420401 | Jacquault et al. | May 1995 | A |
5462009 | Garrigus | Oct 1995 | A |
5652192 | Matson et al. | Jul 1997 | A |
5728195 | Eastman et al. | Mar 1998 | A |
5736092 | Apte et al. | Apr 1998 | A |
5759230 | Chow et al. | Jun 1998 | A |
5886326 | Tang | Mar 1999 | A |
6232264 | Lukehart et al. | May 2001 | B1 |
6280802 | Akedo et al. | Aug 2001 | B1 |
6387494 | Yanagida et al. | May 2002 | B1 |
6416862 | Kogoi et al. | Jul 2002 | B1 |
6501059 | Mast | Dec 2002 | B1 |
6569397 | Yadav et al. | May 2003 | B1 |
6833019 | Lewis, III et al. | Dec 2004 | B1 |
7033416 | Kurihara et al. | Apr 2006 | B2 |
7084408 | Kimball et al. | Aug 2006 | B1 |
7087100 | Lewis et al. | Aug 2006 | B2 |
7211236 | Stark et al. | May 2007 | B2 |
7423512 | Reitz et al. | Sep 2008 | B1 |
20030108683 | Wu | Jun 2003 | A1 |
20030143153 | Boulos et al. | Jul 2003 | A1 |
20030145681 | El-Shall et al. | Aug 2003 | A1 |
20040009118 | Phillips et al. | Jan 2004 | A1 |
20040025635 | Kurihara et al. | Feb 2004 | A1 |
20040255721 | Lewis, III et al. | Dec 2004 | A1 |
20050000950 | Schroder et al. | Jan 2005 | A1 |
20050109159 | Kim et al. | May 2005 | A1 |
20050142059 | Kim et al. | Jun 2005 | A1 |
20070101824 | Drzal et al. | May 2007 | A1 |
20070231234 | Ravi et al. | Oct 2007 | A1 |
20070266825 | Ripley et al. | Nov 2007 | A1 |
20080274042 | Wira et al. | Nov 2008 | A1 |
Number | Date | Country |
---|---|---|
2466765 | May 2003 | CA |
4-336423 | Nov 1992 | JP |
WO9316571 | Aug 1993 | WO |
WO 0000311 | Jan 2000 | WO |