1. Field of the Invention
The invention relates generally to methods for making carbon nanotubes and, particularly, to a method for making the branched carbon nanotubes.
2. Discussion of Related Art
Carbon nanotubes (CNTs) were first discovered by S. Iijima (Nature, vol. 354, pp. 56-58, 1991) and were synthesized by T. W. Ebbesen and P. M. Ajayan (Nature, vol. 358, pp. 220-222, 1992). Theoretical studies show that carbon nanotubes exhibit either metallic or semiconductive behavior depending on the radii and helicity of the nanotubes. CNTs have interesting and potentially useful electrical and mechanical properties and offer potential for use in electronic devices such as field emission displays, micro electron sources in vacuum, and nano-scale devices. Particularly, the branched CNTs have the unique electrical and thermal properties due to a three-terminal/three-dimensional tubular structure. Therefore, the branched CNTs can be widely used in the nano-scale integrated circuits.
At present, the traditional methods for making the branched CNTs include an arc-discharge method, a template method, and a metal organic chemical vapor deposition (MOCVD) method. The arc-discharge method has low yield, the template method has a complex process, and the prevalent method is the MOCVD method. The MOCVD method is costly in manufacture due to use of a metal organic gas as a raw material and cannot form the branched CNTs in a predetermined area. Thus, the application of the MOCVD method in the nano-scale integrated circuits is limited.
What is desired is a low-cost, high-yield, and simple method for making the branched CNTs in a predetermined/chosen area/location.
A method for making the branched carbon nanotubes includes steps, as follows: providing a substrate and forming a buffer layer on a surface of the substrate; depositing a catalyst layer on the surface of the buffer layer, the material of the catalyst layer being not infiltrative (i.e., being non-wetting) with the material of the buffer layer; putting the substrate into a reactive device; and forming the branched carbon nanotubes on the surface of the buffer layer and along the surface of the buffer layer by a chemical vapor deposition method.
Compared with the traditional method for making the branched carbon nanotubes, the present method has the follow advantages: (1) low cost, due to the use of acetylene, ethylene, methane or any suitable chemical compound as a raw material source for carbon; (2) a high yield on the verge of 50%; and (3) good electrical conduction, due to the use of the noble metal as the catalyst, which is ultimately located on the distal end of the branched carbon nanotubes. Furthermore, each branched carbon nanotube can be formed on/at a certain location, by patterning the catalyst layer according to, e.g., a photo-etching method.
Many aspects of the present method for making the branched CNTs can be better understood with reference to the following drawings. The components in the drawings are not necessarily to scale, the emphasis instead being placed upon clearly illustrating the present method.
Reference will now be made, in detail, to the drawings to the synthesis of the branched CNTs, according to the present method.
Referring to
(1) providing a substrate 10 and forming a buffer layer 12 directly on (i.e., in contact with) the upper surface of the substrate 10;
(2) depositing a catalyst layer 14 on the surface of the buffer layer 12 and, particularly, in contact therewith;
(3) putting the substrate 10 with the buffer layer 12 and the catalyst layer 14 formed thereon into a reactive device; and
(4) heating the substrate 10 up to a predetermined temperature (i.e., a reaction temperature) in a flow of protective gas, and, after a period of time, introducing a carbon-containing gas, thereby achieving the branched CNTs 16 on the substrate 10.
In step (1), the substrate 10 can, beneficially, be made of glass, silicon, metal etc. The buffer layer 12 can, usefully, be made of alumina and/or silicon dioxide. The buffer layer 12 may, opportunely, be formed by an electron beam evaporation method, a sputtering method, or a thermal evaporation method. A thickness of the buffer layer 12 is more than 1 nanometer (nm). In the present embodiment, the substrate 10 is made of silicon. The buffer layer 12 is an aluminum oxide layer with a thickness of 10 nm and is formed by the electron beam evaporation method.
In step (2), the catalyst layer 14 may, opportunely, be formed by an electron beam evaporation method, a sputtering method, or a thermal evaporation method. The catalyst layer 14 is advantageously made of a noble metal or an alloy of such metals, e.g., gold, silver, copper, and/or platinum or, alternatively, is made of another known catalyst material, such as nickel. A thickness of the catalyst layer 14 is in an approximate range from 0.5 nm to 1.5 nm. At the synthesis temperature of the branched CNTs, the material of the buffer layer 12 and the material of catalyst layer 14 do not infiltrate and/or wet each other. In the present embodiment, the catalyst layer 14 is a gold layer with the thickness of 1 nm and is formed by the electron beam evaporation method.
In step (3), the reactive device is a traditional tube-shaped furnace with a diameter of about 1 inch.
In step (4), the predetermined temperature is selected according to the material of the catalyst layer 14. In the present embodiment, the temperature is about 880° C.-950° C., beneficially, about 900° C.-950° C. The protective gas advantageously includes hydrogen and argon (i.e., a reducing gas and an inert gas), wherein a flux rate of argon is about 0-140 sccm and a flux rate of hydrogen is about 200 sccm, and beneficially, a flux ratio of argon to hydrogen is about 140:200. The period of time for introducing the protective gas is about 10-30 minutes. The carbon-containing gas can, usefully, be acetylene, ethylene, methane, or any suitable chemical compound that contains carbon. The flux rate of the carbon-containing gas is approximately 10-50 sccm, beneficially, 10-25 sccm. The period of time for introducing the carbon-containing gas is about 5-30 minutes, opportunely, 15 minutes. In the present embodiment, acetylene is used as the carbon-containing gas.
Referring to
Firstly, the catalyst layer 14 is melted when the substrate 10 is heated up, as in step (4) mentioned above. The catalyst layer 14 is rearranged into a number of catalyst balls (i.e., due to the relative surface tension between the catalyst material and the buffer layer 12), and then the catalyst balls are movable on and along the surface of the buffer layer 12. The catalyst material is driven to form multiple catalyst balls because the material of the buffer layer 12 and the material of catalyst layer 14 do not wet each other.
Secondly, the carbon-containing gas decomposes upon contacting surfaces of the catalyst balls, and then the CNTs are formed thereon. The catalyst balls are movable, and thus the CNTs are formed along the surface of the buffer layer 12, following the movement pattern/trail of the catalyst balls. Each catalyst ball is advantageously located on a distal end (i.e., free tip) of each CNT, but, depending on the catalyst material used, such a catalyst ball could be located at the bottom end of a given CNT, adjacent the buffer layer 12.
Thirdly, when two catalyst balls encounter and incorporate/join into a new catalyst ball, two CNTs following the movement pattern of those two catalyst balls will connect together. Thereafter, another CNT is formed following the movement pattern of the new catalyst ball, and then a Y-shaped CNT (referring to
Finally, it is to be understood that the embodiments mentioned above are intended to illustrate rather than limit the invention. Variations may be made to the embodiments without departing from the spirit of the invention as claimed. The above-described embodiments illustrate the scope of the invention but do not restrict the scope of the invention.
Number | Date | Country | Kind |
---|---|---|---|
2007 1 0074810 | Jun 2007 | CN | national |
Number | Name | Date | Kind |
---|---|---|---|
6325909 | Li et al. | Dec 2001 | B1 |
6837928 | Zhang et al. | Jan 2005 | B1 |
20030118727 | Ting et al. | Jun 2003 | A1 |
20060137741 | Park et al. | Jun 2006 | A1 |
20060228289 | Harutyunyan et al. | Oct 2006 | A1 |
20070224104 | Kim | Sep 2007 | A1 |
20090068461 | Reneker et al. | Mar 2009 | A1 |
Number | Date | Country |
---|---|---|
2002-329723 | Nov 2002 | JP |
2003-238123 | Aug 2003 | JP |
2004-59428 | Feb 2004 | JP |
2007-515364 | Jun 2007 | JP |
2007-175205 | Jul 2007 | JP |
2007-528339 | Oct 2007 | JP |
WO2006057833 | Jun 2006 | WO |
Entry |
---|
Pisana (Physica E 37 (2007) p. 1-5, published online Sep. 7, 2006). |
Kukovitsky (Chemical Physics Letters 317 (2000) 65-70. |
Eun Ju Bae et al.“Single-walled carbon nanotube growth on glass” Nanotechnology vol. (18),No. 1,P015601,Dec. 8, 2006. |
Yun-Hi Lee, et al., “Direct nano-wiring carbon nanotube using growth barrier: A possible mechanism of selective lateral growth” Journal of Applied Physics, May 1, 2002, vol. 91, No. 9, pp. 6044-6050. |
Yunyu Wang et al., Comparison study of catalyst nanoparticle formation and carbon nanotube growth: Support effect, Journal of Applied Physics 101, 124310 (2007). |
Number | Date | Country | |
---|---|---|---|
20080299308 A1 | Dec 2008 | US |