The miniaturization of electronic devices into nanometer scale is an indispensable stage for next-generation semiconductor technology. The first step in accomplishing this goal is to synthesize nano-materials which can be used as building components for nano-devices. Among a variety of nanoscale materials, Y-junction single-walled carbon nanotubes (Y-SWNTs) have attracted much attention due to their potential to be used as future nano electronic devices, such as nano-scale transistors.
Since the energy band gap of a semiconducting SWNT is dependent upon its diameter and chirality, a Y-SWNT having variations in tube diameter and/or chirality between branch and stem will make it possible to produce three-terminal nanoscale devices, where the third terminal can be used for controlling switching, power gain, or other properties associated with semi-conductor devices, such as ambipolar field-effect transistors. The literature contains theoretical predictions concerning the electronic transport characteristics of Y-SWNTs: Andriotis, et al., Physical Review Letters, “Rectification properties of carbon nanotube ‘Y-junctions’”, 87(6):066802 (2001). Although methods for synthesizing Y-junction multiwalled carbon nanotubes (Y-MWNTs) have been developed: Gothard, et al., Nano Letters, “Controlled Growth of Y-Junction Nanotubes Using Ti-Doped Vapor Catalyst”, 4(2):213-217 (2004), at present the literature does not disclose a method of producing Y-SWNTs in a controlled manner. Hence, methods of synthesizing Y-SWNTs are very important for next-generation nanoscale semiconducting device applications.
Disclosed are methods of synthesizing Y-junction single-wall carbon nanotubes that can be manufactured either as metallic or semi-conducting based upon the materials used in the synthesis. The synthesis method disclosed herein is reproducible for producing Y-SWNTs using chemical vapor deposition (CVD) techniques which may be either thermal-CVD or plasma-CVD method. The Y-SWNTs are grown on a substrate, such as silicon, quartz, or metal plates. In a preferred embodiment for forming a field effect transistor, the substrate is first coated with an insulating coating, or has a natural oxide surface, such as SiO2, by a spin coating technique and then the SiO2 coating is air dried at room temperature. If the substrate is aluminum oxide or other suitable insulator that is stable at reaction temperature, the SiO2 layer would not be needed. The coated substrate is then sputtered with or otherwise has nanoparticles of solvent solution, containing a mixture of catalyst metal ions, dopant metal ions and metal oxide nanoparticles, deposited thereon. Another important feature of the methods described herein for forming single-wall Y-branched carbon nanotubes is to include the metal oxide catalyst support material in the catalyst/dopant solution, preferably aluminum oxide and/or magnesium oxide, as nanoparticles. Any metal oxide that is stable at reaction temperature is suitable. The metal oxide is important to maintain the catalyst and dopant metals in contact, and effective, with the leading edge of the forming single-wall nanotubes. Preferred solvents for the catalyst/dopant and metal oxide nanoparticles are methanol and/or ethanol. The catalyst concentration should be in the range of about 1 mg to 500 mg per 100 ml. of solvent; the dopant and metal oxide concentrations should be about 1 mg to 100 mg per 100 ml. of solvent. After the particles are dried, the substrate is loaded into a CVD reactor followed by heating to 600 to 1200° C., preferably 700 to 1000° C. under non-oxidizing conditions, e.g., under a blanket of argon gas. After the temperature in the CVD reactor reaches equilibrium, a hydrocarbon gas, e.g., methane, is injected into the CVD reactor to begin the synthesis of single-walled Y-branched nanotubes.
In order to provide Y-branching on the synthesized single-wall nanotube stems, it is necessary to nucleate a single-walled nanotube on the single-walled nanotube stem. The Y-branched SWNT is nucleated on the stem SWNT by attaching a catalyst particle to the side wall of the stem. The catalyst can be any carbide-forming metal atom such as iron, cobalt, nickel, or the like, preferably iron. In accordance with the process described herein, Y-branched SWNTs are formed by providing a solution of catalyst and dopant in a suitable solvent, such as ethanol, and including a metal oxide catalyst support material, in nanoparticles, in the solution. The dopant metal should have a carbide-forming Gibbs free energy less than that of the catalyst metal, preferably titanium, zircomium or molybdenum, to provide doped iron carbide particles with a stronger driving force for attachment to a side surface of the growing single-wall carbon nanotube stems. The dopant is included with the catalyst in solution, e.g., iron, at a molar ratio of catalyst metal to dopant metal, e.g., Fe/Mo, Fe/Zr, Fe/Ti within the range of 1% to 50%, preferably 5% to 30%. If the catalyst metal is iron, as preferred, the dopant metal is Ti, Zr, Hf, V, Nb, Ta, Cr, Mo, and/or W.
a shows a proposed structure of a Y-SWNT wherein S.C. is an abbreviation for semiconductor.
b and 7 show a schematic of a proposed nanoscale transistor using a Y-SWNT having two semiconducting single-walled nanotubes and a third metallic branch formed by a carbon nanotube.
a, 2b, and 2c show a proposed growth mechanism of Y-branched single walled nanotubes;
a and
a) shows a proposed structure 10 of one example of a Y-SWNT which can be used in the fabrication of three-terminal nanoscale devices. The stem 12 is a single-wall carbon nanotube having an arm-chair conducting structure of hexagonal carbon atoms that form the stem 12, and the Y-branches 14 and 16 are semiconductor single-wall carbon nanotubes having a zig-zag structure. Upon formation, at the juncture of the Y-branches, a portion of the metal oxide 15 contained in the catalyst/dopant/metal oxide solution initially applied to the substrate 17 (
The scanning electron microscopy (SEM) image (
The present invention is directed to a method for forming branched single-walled nanotubes and, in a preferred embodiment, the branched nanotubes are used to form three-terminal nanoscale devices, such as ambipolar field-effect transistors, according to the disclosed method. The disclosed method is a chemical-vapor deposition (CVD) method in which a carbide-forming dopant and a metal catalyst are solubilized in a suitable solvent, such as, deionized water, methanol and/or ethanol and the solution is mixed with metal oxide particles. The solution is deposited as nanoparticles (less than 1 mm. in diameter), for example, by photolithography, onto a substrate coated with, or having, an insulating upper layer, e.g., SIO2, or Al2O3. A hydrocarbon gas, such as methane, is fed to the CVD reactor 40 (
An inert gas flow can be supplied to the reactor 40, via tank 46, to provide a carrier flow for materials into the reactor 40. In the preferred embodiment, the inert carrier gas is argon. Optionally, the carrier gas can include additional materials, such as hydrogen. Flow controller 48 can be used to control the flow of inert gas to the reactor 40.
The reactor 40 also includes an inlet port 49 for the flow of one or more hydrocarbon gases, such as methane, acetylene or ethylene, into the reactor 40. A substrate, such as an insulator-coated, e.g., SiO2-coated substrate 50, and carrying doped and metal oxide-containing catalyst solution, at precise locations, applied, e.g., by photolithography, is delivered directly into the reactor 40, prior to heating the reactor 40 to reaction conditions, in order to form one or more field effect transistors on a single substrate 50. For example, four Y-branched single-wall nanotubes can be grown on substrate 50 (4″ by 4″) to produce four FETs.
The carbon source fed to the reactor 40 is generally a hydrocarbon that can, upon decomposition in the reactor 40, provide the elemental carbon for formation of the nanotubes. For example, in one embodiment, the carbon-containing precursor material can be xylene, ethylene, acetylene, methane, or benzene. The carbon source need not be limited to a hydrocarbon, however, and can be any suitable carbon-containing material that can decompose in the furnace to provide the elemental carbon necessary for growth of the developing nanotubes. The preferred carbon source for forming Y-branched single-walled nanotubes is methane, acetylene and/or ethylene.
According to one particular embodiment of the present invention, the carbon source can be derived, at least partly, from an organic solvent that can also serve as a solvent for one or more of the catalyst, and/or carbide-forming dopant materials, e.g., pure ethanol. According to this embodiment, a catalyst and dopant are dissolved in the organic solvent and the liquid solution containing both, as well as metal oxide nanoparticles, are applied to an insulator-coated, e.g., SiO2-coated silicon, quartz or glass substrate.
The materials fed to the reactor 40 may also include a component that contains a portion of the carbide-forming catalyst, metal oxide and dopant necessary for nucleation of the single-walled nanotubes and nucleation of the nanotube branches, in addition to the catalyst/dopant solution and metal oxide initially patterned, e.g., by photolithography, on the insulator-coated substrate 50. The catalyst can be any suitable metal that forms a metal carbide to initiate nanotube formation in the reactor 40. For example, metallic catalysts such as iron, cobalt, nickel, and the like can be utilized in the reactor 40 to initiate formation of the nanotubes and the Y-branches. In general, the catalyst can be a carbide-forming metal atom, preferably iron. In one particular embodiment, the catalyst-containing material soluble in the solvent, e.g., methanol, can be a metallocene, for instance ferrocene, cobaltocene, nickelocene, and the like.
In accordance with an important feature of the Y-branched SWNT process and articles described herein, the substrate is first patterned with a solution of catalyst and dopant admixed with metal oxide nanoparticles, e.g., by photolithography, in defined areas prior to heating the CVD reactor 40 to the high temperature reaction conditions. Also, to achieve the full advantage of the process described herein, the catalyst/dopant molar ratio, in solution, should be in the range of 0.01 to 0.5 moles of catalyst metal-containing molecule for every mole of dopant metal-containing molecule. The combination of the catalyst metal, carbide-forming dopant metal and the metal oxide catalyzes nucleation of Y-branches of the nanotubes at the side surfaces of the single-wall nanotube stems formed within the reactor in a earlier stage of the process. Without the metal oxide catalyst support particles, the catalyst and dopant metals would not be available to catalyze Y-branch formation.
The carbide-forming dopant, catalyst and metal oxide particles can be supplied in the catalyst/dopant/metal oxide solution in any suitable form, i.e., in a form that can provide the elemental dopant metal and catalyst metal in solution mixed with and metal oxide particles. For example, when molybdenum is the dopant metal, the Mo dopant can be bislacetylacetonado)-dioxo-molybdenum.
The conditions in the CVD reactor 40 during the disclosed process can generally be equivalent to those of other CVD nanotube formation processes as are known in the art. For example, reactor 40 can be heated to a temperature between about 600° C. and about 1200° C., preferably about 700° C. to about 1000° C., more preferably about 850° C. to about 950° C., under non-oxidizing conditions, e.g., under a blanket of argon gas. Within the reactor 40, single-walled stems and single walled Y-branches on the stems of the previously formed nanotubes grow spontaneously in highly ordered arrays on the substrate 50, spin-coated with a SiO2 layer, for instance a quartz substrate 50, or any other suitable substrate material as is generally known in the art.
According to the process described herein, when the catalyst/dopant solution, mixed with metal oxide nanoparticles is deposited onto the surface of the substrate 60 in defined areas, and the CVD reaction is heated to reaction temperature, Y-branches spontaneously form on the developing nanotubes.
The present invention is directed to methods for preparing a catalyst and dopant solution and metal oxide particles on substrates, and to methods of using the catalyst/dopant/metal oxide solutions to grow Y-branched, single-wall carbon nanotubes. An exemplary catalyst/dopant/metal oxide deposition pattern includes a uniform dispersion of catalyst/dopant/metal oxide nanoparticles solution deposited by photolithography on the surfaces of a SiO2-coated substrate 50. In these methods, the insulator-coated substrate, including the catalyst/dopant/metal oxide combination patterned on the surface of the insulator coating is placed into the CVD reactor 40 and heated to a high temperature, preferably 800-1000° C. A carbon-containing gas, e.g., methane, is then passed through the reactor for a period of time. Nanotube growth is catalyzed from the carbon-containing gas by the previously deposited solution of the catalyst, dopant and metal oxide nanoparticles.
An embodiment of a reactor for implementing methods of the present invention includes the heating component or furnace 42 and the tube reactor 40 (
Deposition of the catalyst and dopant solution, mixed with the metal oxide catalyst support particles, by a photolithography process, in one embodiment, can employ multiple photolithographic targets. In one embodiment a plurality of photolithographic targets are used, one target comprising a first catalyst/dopant/metal oxide combination in solution, and a second target comprising a second catalyst/dopant/metal oxide combination in solution.
More generally, the deposition of the catalyst, dopant solution and metal oxide particles onto the insulator-coated substrate can be achieved in any number of conventional techniques such as photolithography, sputtering, evaporation, electro-deposition, laser ablation, and arc evaporation.
A reproducible method of synthesizing Y-SWNTs using chemical vapor deposition (CVD) techniques also may include thermal- and/or plasma-CVD. The substrate on which the catalyst, dopant solution and metal oxide particles are prepared is loaded in a CVD reactor, followed by heating to 600-1200° C. under non-oxidizing conditions—e.g., under a blanket of argon gas. After the temperature reaches equilibrium, a hydrocarbon gas, e.g., methane, is injected into the CVD apparatus to synthesize Y-SWNTs, followed by cooling.
In order to form Y-branching, a branched SWNT should nucleate on a stem SWNT. A method for causing such nucleation is by attaching the doped catalyst particles to the sidewall of stem SWNTs. If iron is used as the catalyst, Fe particles should first be reacted with carbon to form iron (Fe) carbide for proper attachment of Fe particles onto the nanotube wall. However, the 3Fe+C=Fe3C reaction is unfavorable at nanotube growth temperatures (e.g., 700-800° C.) since the Gibbs free energy (ΔGf) for the reaction is positive. Although Gibbs free energy of the reaction at 900-1,000° C. is negative, the absolute value is small (ΔG1,173K=−0.375 kcal/mol), which means less probability of carbide formation. Hence, the key process for Y-junction formation is to dope carbide forming elements to Fe particles and make the catalyst/dopant metals available for Y-branching by including a catalyst/dopant metal oxide stabilizer, e.g., aluminum oxide and/or magnesium oxide. The metal oxide stabilizer must be a metal oxide that itself, is stable at the CVD reactor temperature. Fe particles doped with a carbide-forming dopant, such as Ti, Hf; Mo or the like, forms the dopant metal carbide that is attached by the formation of the dopant metal carbide on the side wall of the nanotube stem, and then a new SWNT nucleates and grows, forming Y-junctions. Forming the dopant metal carbide is much easier than that of forming Fe3C when a carbon nanotube meets a catalyst particle. Doped Fe particles, the afore, have a stronger driving force for being attached to SWNTs than pure Fe particles (
In order to prepare Mo-doped Fe catalyst particles on the substrate, iron (III) nitrate monahydrate, aluminum oxide nanoparticles, and bis(acetylacetonato)-dioxomolybdenum (VI) were dissolved in alcohol. The resultant solution was spread on an SiO2-coated Si substrate by conventional spin coating techniques, and then dried in air at room temperature. Exemplary substrates that can be used for synthesizing Y-SWNTs include Si, quartz, metal plates, and the like. Spin-coating involves rotating the substrate at high speed while depositing the solution onto the substrate.
SEM shows that most of the synthesized SWNTs have branches, forming Y-junctions (
Radial breathing mode (RBM) and two components of the G-band peak in the Raman spectra also confirmed that the Y-SWNTs which were synthesized are composed of SWNTs (
Y-SWNTs are grown successfully by a thermal chemical vapor deposition (CVD) method with Fe/Mo catalyst/dopant and aluminum oxide nanoparticles. The Fe/Mo catalyst/dopant solution is prepared by dissolving Iron (III) nitrate nonahydrate, bis (acetylacetonato)-dioxomolybdenum (VI), and aluminum oxide nanoparticles into methanol following by 30 minutes sonication to form a homogeneous suspension. One drop of the catalyst solution is dropped onto a SiO2/Si substrate which is then loaded in a quartz tube CVD-reactor. Then the temperature of quartz reactor is ramped up to 600-1000° C. in an Ar atmosphere (1000 sccm). After the temperature is stabilized, Ar gas flow is replaced by CH4 and H2 (500 sccm for each gas) for the synthesis of Y-branched SWNTs. Finally the quartz tube reactor is cooled to room temperature in a gas flow of 1000 sccm of Ar.
As discussed above in
The current-voltage (I-V) characteristics of nanotubes using different material is illustrated in
The metallic nanotube, on the other hand, displays a negative breakdown voltage of about −1 volts and a positive turn-on voltage of about +1 volts. The (metallic/MS) nanotube displays an almost linear I-V characteristic for the same gap period (between −1 to +1 volts) but shows a turn-on voltage at about +1 volts, e.g., the current increases slightly more rapidly past +1 volts. A metallic-semiconducting (MS) nanotube, created using a metallic tube portion and semiconducting tube portion coupled at a heterojunction, demonstrates little to no leakage current for a voltage gap between −1 and +1 volts. It has a sharper turn-on voltage at +1 volts and a sharper negative breakdown voltage at −1 volts than the metallic nanotube. The rectification ratio (defined as the ratio of forward to reverse current) for the MS nanotube is about 300-500 at 2V. Therefore, the MS nanotube may provide bi-directional rectifying characteristics.
Procedures for controlling the density of Y-SWNTs have also been developed. By increasing the spin coating speed of the substrate during application of the catalyst/dopant/metal oxide solution from 1,000 revolution per minute (rpm) to 6,000 rpm, the density of Y-SWNTs was decreased from approximately 2.9×108 cm−2 to 5.7×107 per cm2.
The growth direction of Y-SWNTs can also be controlled while the SWNT is being formed by applying an electric field, as described in U.S. Pat. No. 6,837,928 B1, hereby incorporated by reference.
For example, the electrodes 112 and 114 may be patterned (e.g., using photolithography and liftoff) having a length, width and height of about 0.8 cm, 0.3 cm and 50-100 nm, respectively, with a space between the electrodes of about 10 microns. The catalyst/dopant/metal oxide material portions 122 and 124 are patterned as strips at about 5 microns high and 0.4 cm in length. A voltage of between about 3V and 20V is applied to the electrodes 112 and 114, with a resistor (e.g., 40kΩ) being used to limit current. The nanotube 132 is then grown in the CVD chamber at 600-1200° C. using about 720 mL/min of methane gas flow, 500 mL/min of hydrogen gas flow and 12 mL/min of ethylene gas flow, for about 2 minutes. Pure hydrogen gas may also be flowed into the CVD chamber during heating and cooling steps and used to inhibit oxidation of the electrodes 112 and 114.
In one embodiment, the catalyst/dopant/metal oxide solution portions 122 and 124 are patterned using a double-layer photolithography approach, wherein an upper layer (e.g., conventional photoresist) is patterned using a conventional photolithography approach and wells are formed in via plasma etching. The upper layer is then removed via exposure to a high flux of light and subsequent development. Catalyst/dopant/metal oxide solution is then deposited from a methanol suspension into the patterned lower layer, which is followed by liftoff of the lower layer.
Y-SWNTs formed under the above-described process conditions were aligned in the direction of the electric field that was applied during the growth process. Finally, using nano-patterning techniques, catalyst/dopant solution nanoparticles were positioned at desired positions, thus influencing locations where nucleation takes place. Thus, the procedures provide methods for synthesizing Y-SWNTs having controlled density, position, and growth direction.
The present application claims the benefit of provisional application Ser. No. 60/627,355 filed Nov. 12, 2004. The entire text of the priority application is incorporated herein by reference in its entirety.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2005/040995 | 11/14/2005 | WO | 00 | 7/24/2008 |
Number | Date | Country | |
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60627355 | Nov 2004 | US |