The present invention relates to the preparation of metal carbide films.
Metal carbides possess exceptional hardness, high temperature stability, low electrical resistivity, and high resistance to corrosion and oxidation. Titanium carbide, for example, shows excellent hardness, high Young's modulus, low coefficient of friction, and good oxidation resistance. Niobium carbide has high hardness, an extremely high melting temperature (3600 K), and also superconducting properties with a transition temperature of about 11 K. These properties make metal carbides potential candidates for a wide range of applications including light wear coatings, passivation layers, and high temperature electronic materials. Metal carbides have been used in rocket nozzles, optical coatings, electronic contacts, diffusion barriers, drill bits, cutting tools, golf spikes, etc.
For many applications, metal carbides need to be in the form of film. Metal-carbide films have been prepared using various physical and chemical deposition techniques. Some of the physical deposition techniques include pulsed laser deposition, reactive laser ablation, ultrahigh vacuum sputter deposition, high current plasma discharge arc deposition, and co-evaporation in an ultrahigh vacuum system. For example, chemical vapor deposition (“CVD”), electron beam deposition (“EBD”), and ion beam assisted deposition (“IBAD”) have been used to deposit NbC and TiC films.
The present invention provides for a process of preparing metal carbide films. According to the process, a homogeneous coating solution including a soluble metal precursor, a soluble polymer and a suitable solvent is deposited on a substrate. Metals suitable for the formation of metal carbide films according to this invention are scandium, yttrium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, boron, aluminum and silicon. The transition metals are from Groups 3, 4, 5, and 6. Boron and aluminum are from Group 13 and silicon is in Group 14. Carbides of the lanthanides and actinides can be also prepared by the process. The soluble polymer is a polymer that binds to the soluble metal precursor, and may include polyethyleneimine (“PEI”) and PEI derivatives such as carboxylated PEI. The coated substrate is heated in a reducing atmosphere that includes a carbon source. As the coated substrate is heated, the solvent evaporates and the polymer decomposes. After polymer decomposition, the carbon source gas decomposes and a film of metal carbide forms on the substrate.
The present invention also provides a process for preparing metal carbide films. According to the process, a homogeneous coating solution is deposited onto a substrate to form a coated substrate, the coating solution including a soluble metal precursor, a soluble polymer and a suitable solvent, the soluble polymer binding to the soluble metal precursor. The coated substrate is heated in a reducing atmosphere that includes inert gas and argon at temperatures and for times characterized as sufficient to evaporate the solvent and remove the polymer. A carbon source gas is added to the reducing atmosphere and the substrate is heated at temperatures and for times characterized as sufficient to form a metal carbide film on the support. After forming the metal carbide film, the addition of the carbon source gas is discontinued and then the supported metal carbide film is heated at temperatures and for times characterized as sufficient to anneal the metal carbide film.
The present invention also provides for a composite film on the substrate wherein the composite film comprises of niobium carbide and carbon nanotubes, and the composite film has a critical current density (Jc) greater than the Jc of niobium carbide without the carbon nanotubes.
The present invention is concerned with the preparation of metal carbide films. The process involves depositing a homogeneous solution of a metal precursor and soluble polymer in a suitable solvent onto a substrate. The soluble polymer assists in the deposition, thus the process can thus be referred to as a “polymer-assisted deposition” (“PAD”) process. Afterward, the solvent is evaporated and the polymer removed by heating at sufficiently high temperatures under a reducing atmosphere. The solvent evaporates first, and afterward the polymer decomposes. A carbon source gas in the reducing atmosphere reacts with metal on the substrate to form the metal carbide film. The metal carbide film can be amorphous. The metal carbide film can also be highly oriented with a preferred orientation, e.g. the metal carbide film can have a highly ordered structure such as an epitaxial structure. Metal precursors include metals that are suitable for the formation of metal carbide films include scandium, yttrium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, boron, aluminum and silicon. The transition metals are from Groups 3-6. Boron and aluminum are also suitable for forming boron carbide and aluminum carbide, and are from group 13. Silicon is in group 14. Carbides of the lanthanides and actinides may be prepared using the same process.
In an embodiment, after the solution of metal an polymer is deposited on the substrate, the coated substrate is heated under a reducing atmosphere of forming gas, which is a gas made up from about 90% to about 99% Argon and from about 1% to about 10% H2. Hydrogen is the reducing agent. The heating continues until the solvent is evaporated and the polymer decomposes, after which the carbon source is added and the temperature is increased so that the carbon source gas can react with the metal to produce the metal carbide film. After the decomposition, the structure can be annealed at still higher temperature.
In another embodiment, after the solution of metal and polymer is deposited on the substrate, the coated substrate is heated under a reducing atmosphere that includes both the forming gas and the carbon source gas.
In still another embodiment, after the solution is deposited on the substrate, the coated substrate is heated under a reducing atmosphere that includes the carbon source gas but does not include hydrogen or an inert gas.
It is preferable that the initial heating of the substrate with polymer and metal solution deposited thereon be under a reducing atmosphere of forming gas (a gaseous mixture of hydrogen and argon) prior to adding the carbon source gas. It is also preferred for reasons of safety that the reducing atmosphere also includes an inert gas, such as argon, helium, or nitrogen. Argon is a preferred inert gas.
Other gases besides forming gas can be used, i.e. the hydrogen can be replaced with other reducing agents such as, but not limited to, ammonia, formaldehyde, carbon monoxide, and formic acid. It is preferred for reasons of safety that the reducing atmosphere includes inert gas such as argon, helium, and/or nitrogen. Suitable gaseous carbon sources include hydrocarbons (e.g. ethylene, methane, acetylene), and alcohols (e.g. ethanol).
Metal carbide films prepared according to this invention are uniform films, i.e., they are continuous films covering the target substrate. They can also be readily formed as conformal films upon non-planar substrates or surfaces.
The soluble polymer used in the present process binds to the metal precursors through any of various mechanisms such as electrostatic attraction, hydrogen bonding, covalent bonding and the like.
The polymers should be soluble, compatible with the metal precursors, and also undergo a clean decomposition upon heating at high temperatures, e.g., temperatures over about 250° C. Preferred soluble polymers include polyethylenimine (PEI) and PEI derivatives such as a carboxylated-polyethylenimine (PEIC), a phosphorylated-polyethylenimine (PEIP), a sulfonated-polyethylenimine (PEIS), an acylated-polyethylenimine, hydroxylated water-soluble polyethylenimines and the like. The soluble polymer can also be a polymer such as polyacrylic acid, polypyrolidone, and poly(ethylene-maleic acid). Because PEI decomposes completely and cleanly above 250° C. and leaves little or no residual carbon in the film, PEI and PEI derivatives are preferred polymers. Typically, the molecular weight of such polymers is greater than about 30,000.
The solutions of soluble polymer and metal precursor that are used in depositing the polymer and metal on the substrates are homogeneous solutions. By “homogeneous” is meant that the solutions are not dispersions or suspensions, but are actual solutions of the polymer, metal complexes and any metal binding ligands.
The soluble polymer, besides aiding in the deposition, also aids in attaining a suitable viscosity for allowing processing of the metal carbide precursor solution into desired configurations such as films. The desired viscosity can be achieved through controlling the solution concentration of the soluble polymers and by controlling the molecular weight of the polymer. For high quality homogeneous films, polymer concentrations and the polymer ratio to metal components should be maintained at a proper balance. The rheology of the metal carbide precursor solution can also be important for the morphology and quality of the final metal carbide films. In order to form smooth films, the polymer solution must have suitable rheological properties so that any spin-coated film has no undesired patterns associated with polymer rheological properties.
The soluble polymer also functions as binding agent to metal in the precursor solution in assisting the formation of the deposited polymer-and-metal containing film and ultimately a metal carbide film. The polymer should have suitable interactions with metal ions that prevent phase separation during deposition. Thereafter, the deposited polymer-metal composite films are heated at high temperatures (calcined), e.g., at temperatures above about 450° C. to obtain the metal carbide films. The soluble polymer selection should also have a clean decomposition under such calcination conditions so that the final metal carbide film can be free of side products.
Metals suitable for the formation of metal carbide films according to this invention are scandium, yttrium, titanium, zirconium, hafnium, vanadium, niobium, tantalum, chromium, molybdenum, tungsten, boron, aluminum and silicon. The transition metals are from Groups 3-6, boron and aluminum are from group 13, and silicon is from group 14 of the periodic table of the elements. Carbides of the lanthanide metals and the actinide metals may also be prepared using the process of this invention. For purposes of this invention, boron and silicon is being treated as metals and therefore a silicon carbide film, for example, for purposes of this invention is treated as a metal carbide film, and a silicon containing precursor is treated as a metal containing precursor the same way that a titanium containing precursor, a niobium containing precursor, a vanadium containing precursor, and a tantalum containing precursor are treated as metal containing precursors.
The metal carbide films prepared by the present process can include a metal carbide with a single metal, can be a metal carbide with two metals or three metals or may be a metal carbide including four or more metals. Among the metal carbides that can be prepared by the present process are included metal carbides from Groups 3, 4, 5, and 6 as well as the carbides of silicon, boron, and aluminum. These carbides include silicon carbide, titanium carbide, niobium carbide, vanadium carbide, tungsten carbide, and tantalum carbide. Films with two metals include titanium carbide/niobium carbide, titanium carbide/vanadium carbide, titanium carbide/tantalum carbide, niobium carbide/vanadium carbide, niobium carbide/tantalum carbide, vanadium carbide/tantalum carbide, and the like. Films with three metals include titanium carbide/niobium carbide/vanadium carbide. Films with four metals include titanium carbide/niobium carbide/vanadium carbide/tantalum carbide.
The solvent for dissolution of the soluble polymer can be, e.g., water, lower alcohols such as methanol, ethanol, propanol and the like, acetone, propylene carbonate, tetrahydrofuran, acetonitrile, acetic acids and mixtures thereof such as water and ethanol and the like. As the soluble polymer used in the present invention includes binding properties for the metals or metal precursors used in formation of the metal carbide films, the polymer can help provide the necessary solubility to the respective metals, e.g., metal precursors.
The starting solution is typically maintained at ambient temperatures from about 15° C. to about 30° C., more usually from about 20° C. to about 25° C. Within those temperature ranges and above the higher temperature, the materials added to the solution are soluble. In preparation of solutions used in the present process, the solutions using a polyethylenimine as the metal binding polymer can be filtered prior to use to remove any non-soluble components. Typically, a precursor solution of containing metal and a polyethyleneimine is filtered using an Amicon ultrafiltration unit containing an untrafiltration membrane designed to pass materials having a molecular weight of less than about 3,000 g/mol (e.g., unbound metal, smaller polymer fragments and the like) while retaining the desired materials of a larger size. Ultrafiltration allows for removal of any unwanted salts such as cations, anions or other impurities.
The metal ratio can be controlled through appropriate addition of metal precursors to a solvent used in the deposition. Such solutions can generally have a shelf life of more than a year.
The homogeneous coating solution can be deposited on a desired substrate, such as a sapphire substrate or a silicon substrate, e.g., by spray coating, dip coating, spin coating, ink jet printing and the like. After deposition of the homogeneous coating solution onto the substrate, the deposited coating must be heated at high temperatures (i.e. calcined) of from about 250° C. to about 1300° C., preferably from about 400° C. to about 1200° C. for a period of time sufficient to remove the polymer and to form the metal carbide film. Heating times may be varied and may be longer depending upon the thickness of the deposited film.
Optionally, the deposited coating can be initially dried by heating to temperatures of from about 50° C. to about 150° C. for from about 15 minutes to several hours, preferably for less than one hour. The deposited polymer-metal carbide film undergoes removal of a percentage of volatile species, mostly water, during such an initial drying stage.
The resultant metal carbide films from the present process have been optical quality films in that they are highly smooth films with a mirror-like appearance. Many of the films have been found to be epitaxial in structure. For example,
In an aspect of the present invention, composites can be prepared including the various metal-containing films as described with various additional additives to provide tailoring of the material properties. Included among the possible additives are nanofibers such as carbon nanotubes. The carbon nanotubes affect the properties of the film, such as the critical current density of a superconducting film. Before the composite material, some terminology related to current, current density, critical current, and critical current density will be described.
Current is the rate of flow of electric charge, usually represented by the equation I=Q/t wherein I is the current in amperes, Q is the charge in coulombs, and t is the time in seconds. The current density is the current divided by the cross sectional area through which it flows. The current therefore, is current density multiplied by the cross sectional area through it flows. Critical current is critical current density multiplied by cross sectional area. Critical current density (“Jc”) is the maximum current density that can be transported by a particular superconductor material without losing its superconductivity. If the current through a superconductor increases beyond the critical current for that superconductor, the superconductivity vanishes and the material loses its superconductivity and returns to a non-superconductive state. The critical current density is one of the most important electrical parameters of a superconductor because a large current is often needed for many applications. When the superconducting properties of materials are compared, those materials having a greater critical current density (Jc) use a smaller cross-sectional area, or smaller volume, to carry the same amount current compared to materials with a smaller Jc. Using materials with a higher Jc reduces the cost of raw materials and cost of producing the superconducting components.
In an embodiment, a composite film of niobium carbide and carbon nanotubes, using an aligned array of carbon nanotubes was prepared. The critical current density (“Jc”) of the film was measured and compared to the Jc of a film of niobium carbide prepared without the carbon nanotubes. The Jc of the composite film was significantly higher than the Jc of the film without the carbon nanotubes.
The present invention enables the processing of metal carbide films with convenience and flexibility required in industrial fabrication. This process involves making metal carbide films from solutions - optionally in an organic solvent-free process. Films of titanium carbide, niobium carbide, vanadium carbide, tungsten carbide, tantalum carbide, and silicon carbide have been prepared using polymer-assisted deposition (“PAD”) techniques. X-ray diffraction measurement indicates that the titanium carbide and niobium carbide films on r-plane and c-plane sapphire substrates are preferentially oriented along the (100). They are also epitaxial as confirmed from x-ray -scans of the (101) diffraction of the films and transmission electron microscopy.
The polymer is used to bind metals and metal precursors. This allows the removal of any unwanted anions or cations by filtration, e.g., through an Amicon ultrafiltration unit, and brings multiple metals together in a homogeneous manner at a molecular level. This also prevents selective precipitation of unwanted metal phases as a portion of the water can be removed and the metals concentrated within the remaining solution. The present invention can control the relative metal concentrations at the molecular level for mixed metal carbides (TiC/NbC, for example). This can be done, for example, by adding a single polymer (such as carboxylated polyethyleneimine) to a solution containing simple salts (such as nitrate) of two or more metals in the correct ratio. If the binding constant is high for both metals then they will remain in the correct ratio during filtration and concentration of the polymer. Alternatively, each metal can be bound to a polymer, and then the metals can be mixed and the resulting solution can be concentrated and then examined by ICP to determine metal content and then mixed appropriately prior to spin coating. Different polymers and different solvents can be used for different metals in this system.
The present invention is more particularly described in the following examples which are intended as illustrative only, since numerous modifications and variations will be apparent to those skilled in the art.
A precursor solution for making titanium carbide films was prepared as follows: 12 grams (“g”) of hexafluorotitanic acid (H2TiF6, ALDRICH, 99.9%, 60% in water) was added to 7.5 g of a solution of polyethyleneimine (“PEI”) (purchased from BASF CORPORATION, Clifton N.J., used without further purification) and 40 mL of water purified to 18 MΩ.cm using a MILLI-Q water treatment system. The resulting solution was purified by ultrafiltration, which was carried out using Amicon stirred cells and a 3,000 molecular weight cut-off ultrafiltration membrane under 60 psi argon pressure. Titanium analysis was conducted using a HORIBA JOBIN YVON ULTIMA II inductively coupled plasma-atomic emission spectrometer (“ICP-AES”) following the standard SW846 EPA (Environmental Protection Agency) method 6010 procedure. Analysis showed that the final Ti precursor solution was 496 millimolar (“mM”) in Ti.
A precursor used for making niobium carbide films was prepared as follows: NbCL5 (>99% pure), NH4OH, and 20% HF were dissolved in water where the water was purified using the Milli-Q water treatment system. Ultrafiltration was carried out under 60 psi nitrogen pressure using Amicon stirred cells with a 3000 molecular weight cut-off. In detail, 2 g of NbCl5 were converted to Nb(OH)5 by addition of ammonium hydroxide into the solution. The Nb(OH)5 was then dissolved in 30 mL of deionized water and 7.5 mL of 20% HF. PEI was then added in 31 g aliquots (total of 3.0 g) and mixed after each addition. After stirring, the solution was placed in an Amicon filtration unit containing a filter designed to pass materials with molecular weight <3,000 g/mol. The solution was diluted 3 times to 200 mL and then purified by ultrafiltration, which resulted in a final volume of about 35 mL in volume. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 400 mM in Nb.
A precursor solution for making tantalum carbide films was prepared as follows: tantalum chloride was dissolved in water Ammonium hydroxide was added, which resulted in precipitation of tantalum hydroxide (Ta(OH)5). The precipitate was rinsed with copious amounts of deionized water to remove chloride from the precipitate. The precipitate was then dissolved in 20% HF solution to form a tantalum fluoride complex. PEI was added to this solution, and afterward, ultrafiltration was carried out using Amicon stirred cells and a 3,000 molecular weight cut-off ultrafiltration membrane under 60 psi argon pressure. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 214 mM in tantalum.
A precursor solution for making vanadium carbide films was prepared as follows: 2 g sodium vanadate was dissolved in 40 ml of water containing 2 g of PEI polymer. The resulting solution was purified by ultrafiltration using Amicon stirred cells and a 3,000 molecular weight cut-off ultra filtration membrane under 60 psi argon pressure to give a solution with 134 mM for vanadium concentration as measured by inductively coupled plasma-atomic emission spectroscopy.
A precursor solution for making silicon carbide films was prepared as follows: 12 g of fluorosilcic acid, H2SiF6 (25 wt % H2SiF6 in water) was mixed with 3.0 g PEI in 40 mL of water. After stirring, a few drops of 20% HF solution were added to remove any cloudiness, and the resulting solution was placed in an Amicon filtration unit containing a filter designed to pass materials having a molecular weight <3,000 g/mol. The solution was diluted to 200 mL, and then purified by ultrafiltration, which resulted in a final volume of 35 mL in volume. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 456 mM in Si.
A precursor solution for making silicon carbide films was prepared as follows: 8 g of water glass (50 wt % sodium silicate in water) was added to 30 mL of water. PEI (7 g) was then added and the solution mixed until the PEI dissolved. The solution was placed in an Amicon filtration unit containing a filter designed to pass materials having a molecular weight <3,000 g/mol. The solution was diluted to 200 mL and then concentrated to approximately 50 mL in volume; this procedure was repeated 5 times to remove the sodium. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 473 mM in Si.
A precursor solution for making tungsten carbide films was prepared as follows: An amount of 7.0 grams of polyethylenimine was dissolved in 70 mL of water. An amount of 8 g of sodium tungstate was added and the resulting solution was titrated to pH 4 using 10% HCl. The resulting solution was stirred, then filtered through CELITE® and diatomaceous earth, and then placed in an Amicon filtration unit containing a PM 10 filter designed to pass materials having a molecular weight <10,000 g/mol. The solution was diluted to 200 mL and then purified by untrafiltration which resulted in concentrating the solution to a volume of 80 mL. This process was repeated three times to remove the unwanted sodium. Inductively coupled plasma-atomic emission spectroscopy showed that the final was 257 mM in W.
A titanium carbide film was prepared as follows: precursor solution from Example 1 was spin-coated on a c-plane sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour. The temperature was held at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film is about 40 nm for one spin-coat.
A titanium carbide film was prepared as follows: precursor solution from Example 1 was spin-coated on a sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in forming gas (10 sccm) then the gas was changed to mixed gases of ethylene (10 sccm) and in forming gas (10 sccm) and annealed at 650 ° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film is about 40 nm for one spin-coat.
A titanium carbide film was prepared as follows: precursor solution from Example 1 was spin-coated on a sapphire substrate at 3000 rpm for 20 s, respectively. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The titanium carbide coated sapphire was spin-coated with another layer of Ti precursor solution at 3000 rpm for 20 s.
The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 80 nm for two spin-coats.
A tantalum carbide film was prepared as follows: precursor solution from Example 3 was spin-coated on a sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film is about 40 nm for one spin-coat.
A vanadium carbide film was prepared as follows: precursor solution from Example 4 was spin-coated on sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A niobium carbide film was prepared as follows: precursor solution from Example 2 was spin-coated on a (006) sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A niobium carbide film was prepared as follows: precursor solution from Example 2 was spin-coated on sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in ethylene (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of the film was about 40 nm for one spin-coat.
A niobium carbide film was prepared as follows: precursor solution from Example 2 was spin-coated on sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in ethylene (10 sccm) and hydrogen gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in hydrogen gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 5 was spin-coated on a silicon substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in forming gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 5 was spin-coated on a silicon substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 5 was spin-coated on a quartz substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in forming gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 6 was spin-coated on a silicon substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in forming gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 urn for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 6 was spin-coated on a silicon substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film was about 40 nm for one spin-coat.
A silicon carbide film was prepared as follows: precursor solution from Example 6 was spin-coated on a quartz substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in forming gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace. The thickness of film is about 40 nm for one spin-coat.
A mixed metal carbide film of titanium carbide and vanadium carbide was prepared as follows: A 1:1 molar ration of the precursor solutions from Example 1 and Example 4 were mixed together and then this solution was then spin-coated onto a sapphire substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in Ar gas (10 sccm) by increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace.
A composite film of niobium carbide and carbon nanotubes was prepared as follows: an amount of the precursor solution of Example 2 was allowed to permeate through an aligned array of carbon nanotubes. The resulting film was heated to 650° C. at a rate of 10° C./min in mixed gases of ethylene (10 sccm) and forming gas (10 sccm) and annealed at 650° C. Thereafter, the mixture gases were switched off, and the Ar gas flow or forming gas was turned on. The temperature was ramped to 1000° C., and the sample was annealed for 3 h. Finally, the temperature of the furnace was allowed to decrease to room temperature naturally.
A composite film of niobium carbide and carbon nanotubes was prepared as follows: precursor solution from Example 2 was allowed to permeate through a carbon nanotube aligned array. The sample was heated to 650° C. in ethylene (10 sccm) and annealed at 650° C. Thereafter, the mixture gases were switched off, and the Ar gas flow or forming gas was turned on. The temperature was ramped to 1000° C., and the sample was annealed for 3 h. Finally, the temperature of the furnace was allowed to decrease to room temperature naturally. The material obtained was basically identical to that seen in example 23.
A tungsten carbide film was prepared as follows: precursor solution from Example 7 was spin-coated on a silicon substrate at 3000 rpm for 20 s. The film was heated to 650° C. at a rate of 10° C./min in methane gas (10 sccm) and annealed at 650° C. for 2 h. The sample was then annealed in argon increasing the temperature from 650° C. to 1000° C. in one hour and staying at 1000° C. for 3 h. Finally, the temperature of the furnace was decreased to room temperature by turning off the power supply to the furnace.
A precursor solution for making yttrium carbide films was prepared as follows: an amount of 1.0 gram of ethylenediaminetetraaceticacid (“EDTA”) was placed in a 50 mL Falcon tube and 25 mL of water were added. The EDTA does not dissolve at this stage. An amount of 1.0 gram of polyethylenimine (from BASF) was added to the solution and the solution was agitated until the EDTA and the polyethylenimine were in solution. Then 1.36 grams of yttrium nitrate hexahydrate were added. The solution was stirred and then placed in an Amicon ultrafiltration unit containing a PM 10 ultrafiltration membrane designed to pass materials having a molecular weight <10,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration which resulted in final volume of 10 mL. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution had 15.3 mg/mL of Y.
A precursor solution for making zirconium carbide films was prepared as follows: An amount of 1.0 grams of dipotassium ethylenediaminetetraacetic acid was dissolved in 30 mL of water. To this solution was added 2.0 grams of zirconyl nitrate (35 wt % in water) and the solution was stirred. An amount of 1.0 gram of polyethylenimine was then added to the solution and the solution was stirred. The resulting solution is clear and has a pH of 8.0. This solution was placed in an Amicon ultrafiltration unit containing a PM 10 ultrafiltration membrane designed to pass materials having a molecular weight <10,000 g/mol. The solution was diluted to 200 mL with absolute ethanol and then subjected to untrafiltration which resulted in a volume of 10 mL Inductively coupled plasma-atomic emission spectroscopy showed that the final solution had 19.3 mg/mL of Zr.
A precursor solution for making aluminum carbide films was prepared as follows: Fluorinated polyethyleneimine polymer was prepared by slowing adding an amount of 5 mL of 48% hydrofluoric acid to an amount of 10 g of polyethyleneimine in 40 mL water while maintaining pH at 7. An amount of 2.0 g of aluminum nitrate hydrate was added to 3 g of the fluorinated polyethyleneimine polymer in 40 ml, water. The final concentration of Al was 200.6 mM.
A precursor solution for making aluminum carbide films was prepared as follows: An amount of 2.0 grams of EDTA was placed in a 50 mL Falcon tube and 40 mL of nanopure water were added. The EDTA does not dissolve at this stage. An amount of 2.6 g of aluminum nitrate nonahydrate was added to the solution, followed by the addition of 2.2 g of polyethylenimine (BASF) and the solution was agitated until everything was dissolved. The solution was stirred and then placed in an Amicon filtration unit containing a PM 10 filter designed to pass materials having a molecular weight <10,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration, which concentrated it to a volume of 10 mL The final concentration of aluminum was 119 mM.
A precursor solution for making boron carbide films was prepared as follows: An amount of 0.34 g of potassium borohydride was added to a solution of polyethylenimine (0.35 g) in 10 mL of water. The mixture was stirred until no solid remained, and was then placed in an Amicon filtration unit containing a PM 10 filter designed to pass materials having a molecular weight <10,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration, which resulted in a volume of 10 mL. The final concentration of aluminum was 105 mM.
A precursor solution for making hafnium carbide films was prepared as follows: 2.0 g of HfOCL2 (ALDRICH, 99.99% pure), 2.0 g HEDTA, 2.0 grams polyethylenimine polymer (BASF), and concentrated ammonium hydroxide (FISHER) in deionized (18 MOhms) H2O were mixed together until a clear solution was produced. The resulting solution was filtered through a 0.45 micron filter, diluted to 200 mL with nano pure water, and purified by Amicon filtration with a 3,000 MW cut-off filter. The final concentrated solution was 163 mM Hf, determined by ICP/AES. This solution was rotovapped to further concentrate it, resulting in a final concentration of 250 mM Hf.
A precursor solution for making lanthanum carbide films was prepared as follows: The La precursor was made by adding 2.6 grams lanthanum nitrate hydrate (99.999%, ALDRICH) to 20-mLs water purified to 18Ω and dissolved. 2 grams EDTA (Aldrich 99.995%)was added to the solution, followed by 2.5 grams PEI purchased from BASF Corporation of Clifton, N.J., and used without further purification. 2-mLs concentrated NH4OH was added to facilitate dissolution. Ultrafiltration was carried out using Amicon stirred cells and 10,000 molecular weight cut-off ultrafiltration membrane under 60 psi argon pressure. Metal analysis was conducted with a Horiba Jobin Yvon Ultima II inductively coupled plasma-atomic emission spectrometer (ICP-AES) following the standard SW846 EPA (Environmental Protection Agency) method 6010 procedure. The resulting La concentration was 220 mM.
The scandium precursor solution was made by adding 3.0 grams scandium trichloride (99.9%, STREM) to 20-mLs water purified to 18Ω and dissolved. 5.92 grams EDTA (Aldrich 99.995%) were added to the solution, followed by 5.82 grams PEI purchased from BASF Corporation of Clifton, N.J., and used without further purification. Ultrafiltration was carried out using Amicon stirred cells and 10,000 molecular weight cut-off ultrafiltration membrane under 60 psi argon pressure. Metal analysis was conducted with a Horiba Jobin Yvon Ultima II inductively coupled plasma-atomic emission spectrometer (ICP-AES) following the standard SW846 EPA (Environmental Protection Agency) method 6010 procedure. The resulting Lu concentration was 145 mM at pH 6.94.
A solution including titanium and hydrogen peroxide and PEI and EDTA was prepared as follows: A solution of soluble titanium was prepared by placing 2.5 grams of 30% hydrogen peroxide into 30 mL of water and then slowly adding 2.5 grams of titanium tetrachloride. Small aliquots of the titanium solution were then added to a solution containing 1 g EDTA and 1 g of PEI in 40 mL of water. The pH was monitored and as the pH decreased below pH 3.5, aliquots of 10% NaOH were added to raise the pH to pH 7.5. This process was repeated until addition of the titanium solution resulted in a precipitate that would not dissolve. The precipitate was removed by filtration and the filtrate was placed in an Amicon ultrafiltration unit containing an ultrafiltration membrane designed to pass materials having a molecular weight <30,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration which resulted in a volume of 10 mL This dilution and ultrafiltration process was repeated two more times. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 461mM Ti.
A solution including boron and PEI and EDTA was prepared as follows. Boric acid (1 g) was added to a solution of 1 g of PEI in 40 mL of water. The solution was then placed in an Amicon ultrafiltration unit containing an ultrafiltration membrane designed to pass materials having a molecular weight <30,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration, resulting in a volume of 10 mL. This dilution and ultrafiltration process was repeated two more times. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 727 mM B.
A solution including vanadium EDTA and PEI was prepared as follows: Vanadyl sulfate hydrate (0.6g) was added to a solution of 1.0 g EDTA in 40 mL of water. The solution was mixed and 1.0 g of PEI was added. The solution was then filtered through a 0.45 micron filter and placed in an Amicon ultrafiltration unit containing an ultrafiltration membrane designed to pass materials having a molecular weight <30,000 g/mol. The solution was diluted to 200 mL and then subjected to ultrafiltration resulting in a volume of 10 mL, and this dilution and ultrafiltration process was repeated three more times. Inductively coupled plasma-atomic emission spectroscopy showed that the final solution was 218 mM V.
STATEMENT REGARDING FEDERAL RIGHTS This invention was made with government support under Contract No. DE-AC52-06NA25396 awarded by the U.S. Department of Energy. The government has certain rights in the invention.