The embodiments disclosed herein relate to hetero-nanostructures for efficient solar energy conversions, and more particularly to the fabrication of nanonet-based hematite hetero-nanostructures and methods of using same for water splitting.
Semiconductors hold great promise for high-efficiency solar water splitting as a form of solar energy harvesting and storage. Since the first demonstration using TiO2, a large number of materials have been studied for this application. Among them, hematite (alpha-Fe2O3) stands out for at least two important reasons: the bandgap of hematite (2.02.2 eV) is close to the optimum requirement for a single junction system; and hematite consists of two abundant elements and therefore is low cost and amendable to large scale implementations. Hematite has been studied for solar water splitting to generate hydrogen fuel with high theoretical conversion efficiency. Despite intense effort, however, research on using hematite for solar water splitting is progressing at a slow pace because of several challenges presented by the material's intrinsic properties. For instance, the charge diffusion distance of Fe2O3 is notoriously short—on the order of a few to tens of nanometers—making it extremely difficult to collect photogenerated charges. Much ongoing effort focuses on addressing this problem by doping Fe2O3 to increase the charge diffusion distance, or by innovating its morphology to improve charge collection, or both.
Nanonet-based hematite hetero-nanostructures for solar energy conversions and methods of fabricating same are disclosed herein. According to aspects illustrated herein, there is provided a hetero-nanostructure that includes a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle, the plurality of nanobeams including a conductive silicide core having an n-type photoactive hematite shell.
According to aspects illustrated herein, there is provided a device for splitting water to generate hydrogen and oxygen that includes a first compartment having a two-dimensional hetero-nanostructure, the hetero-nanostructure having a plurality of connected and spaced-apart nanobeams, each nanobeam substantially perpendicular to another nanobeam, the plurality of nanobeams including an n-type photoactive hematite shell having a conductive core; and a second compartment having a p-type material, wherein the first compartment and the second compartment are separated by a semi-permeable membrane.
According to aspects illustrated herein, there is provided a method of fabricating a nanonet-based hematite hetero-nanostructure that includes performing chemical vapor deposition so as to fabricate a two-dimensional conductive silicide nanostructure, wherein one or more gas or liquid precursor materials carried by a first carrier gas stream react to form the nanostructure, and wherein the nanostructure has a mesh-like appearance and includes a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle; annealing the nanostructure; and performing atomic layer deposition so as to deposit a conformal crystalline hematite around the nanostructure, wherein the film ranges from about 10 nm to about 40 nm, and wherein one or more gas or liquid precursor materials carried by a second carrier gas stream react to form the hematite hetero-nanostructure.
The presently disclosed embodiments will be further explained with reference to the attached drawings, wherein like structures are referred to by like numerals throughout the several views. The drawings shown are not necessarily to scale, with emphasis instead generally being placed upon illustrating the principles of the presently disclosed embodiments.
While the above-identified drawings set forth presently disclosed embodiments, other embodiments are also contemplated, as noted in the discussion. This disclosure presents illustrative embodiments by way of representation and not limitation. Numerous other modifications and embodiments can be devised by those skilled in the art which fall within the scope and spirit of the principles of the presently disclosed embodiments.
Research on using hematite (Fe2O3) to absorb solar light and split water is moving at a slow pace despite the positive prospect of hematite having the suitable bandgap and being low cost, and the limiting factor has been the intrinsic physical and chemical properties of this material. The hetero-nanostructures of the present disclosure tackle these deficiencies by combining a highly conductive interfacing material with a photoactive Fe2O3 coating. The highly conductive interfacing material acts as a structural support for the uniform thin Fe2O3 coating, and as a dedicated charge transport pathway with high surface area. The interfacing material provides superior conductance, thus carrying away collected electrons once illuminated, but also improves (at least maintains) the surface-to-volume ratio for good light absorption and chemical reactions. The interfacing material is in the nanoscale range (for high surface area), is electrically connected (for efficient charge transport), and is intrinsically conductive. The interfacing material absorbs light to a limited extent, leaving most of the optical energy to the hematite shell. Interfacing materials include, but are not limited to, vertically-aligned metal nanowires, vertically-aligned transparent conductive oxides (tin-doped indium oxide (ITO) nanowires and aluminum doped zinc oxide (AZO) nanowires and nanotubes), unaligned metal nanowires, unaligned transparent conductive oxides, nanonets (NNs), porous carbon, like those used in Li ion battery anodes, heavily doped Si nanostructures, silicides of titanium (TiSi2), cobalt (CoSi2), and nickel (NiSi), and sulfides, such as copper sulfide (Cu2S)
In an embodiment, the present disclosure relates to the combination of photoactive ultrathin hematite with highly conductive complex titanium disilicide nanonets to yield Fe2O3/TiSi2 hetero-nanostructures of the present disclosure. Atomic layer deposition is used to synthesize ultrathin hematite with excellent control over film composition and uniformity. The ultrathin hematite is photoactive, even with film thickness less than 20 nm. The titanium disilicide nanonets, with high surface area and excellent conductivity, enhance the light absorption and charge transfer. The Fe2O3/TiSi2 hetero-nanostructures of the present disclosure have great potential to significantly advance the efficiency of solar water splitting by improving the hematite and nanonets at the same time.
The lowest resistivity of Si one can achieve is around 1 mΩ·cm, about 10 times higher than that of TiSi2. The interfacing materials to be used have electron energy levels (Fermi level) similar to those of hematite. In an embodiment, the interfacing materials to be used do not have a significant mismatch with hematite in terms of electron energy levels. Otherwise, a significant barrier would be created, thereby lowering the efficiency. In an embodiment, the interfacing material is TiSi2. The hematite shell is able to absorb solar light, excite and separate electrons and transfer the separated charges (electrons or holes) to the solution to create H2 (or O2).
In an embodiment, the hetero-nanostructures of the present disclosure are useful for high efficiency solar energy conversion. In an embodiment, the hetero-nanostructures of the present disclosure are used as photoelectrochemical cells for H2 production from H2O splitting by harvesting solar energy. In an embodiment, the hetero-nanostructures of the present disclosure are used as photovoltaic solar cells. In an embodiment, the hetero-nanostructures of the present disclosure are used as photocatalyst for pollutants treatments. In an embodiment, the hetero-nanostructures of the present disclosure are used to enhance the efficiency of water splitting to generate hydrogen fuel. In an embodiment, the hetero-nanostructures of the present disclosure are used as a battery electrode. In an embodiment, the hetero-nanostructures of the present disclosure are used as an anode material for a Li-ion battery.
Silicides are highly conductive materials formed by alloying silicon with selected metals. Titanium silicide (TiSi2) is an excellent electronic material and is one of the most conductive silicides (resistivity of about 10 micro-ohm-centimeters (μΩ·cm)). TiSi2 has recently been demonstrated to behave as a good photocatalyst to split water by absorbing visible lights, a promising approach toward solar H2 as clean energy carriers. Better charge transport offered by complex structures of nanometer-scaled TiSi2 is desirable for nanoelectronics and solar energy harvesting. Capabilities to chemically synthesize TiSi2 are therefore appealing. Synthetic conditions required by the two key features of complex nanostructures, low dimensionality and complexity, however, seem to contradict each other. Growth of one-dimensional (1D) features involves promoting additions of atoms or molecules in one direction while constraining those in all other directions, which is often achieved either by surface passivation to increase energies of sidewall deposition (such as solution phase synthesis) or introduction of impurity to lower energies of deposition for the selected directions (most notably the vapor-liquid-solid mechanism). Complex crystal structures, on the other hand, require controlled growth in more than one direction. The challenge in making two-dimensional (2D) complex nanostructures is even greater as it demands more stringent controls over the complexity to limit the overall structure within two dimensions. The successful chemical syntheses of complex nanostructures have been mainly limited to three-dimensional (3D) ones. In principle, 2D complex nanostructures are less likely to grow for crystals with high symmetries, e.g. cubic, since various equivalent directions tend to yield a 3D complex structure; or that with low symmetries, e.g. triclinic, monoclinic or trigonal, each crystal plane of which is so different that simultaneous growths for complexity are prohibitively difficult.
In an embodiment, a chemical vapor deposition (CVD) system is used for the fabrication of complex two-dimensional (2D) conductive silicide nanostructures of the presently disclosed embodiments. An example of a suitable system for the fabrication 2D conductive silicide nanostructures of the present disclosure is disclosed in co-pending U.S. application Ser. No. 12/546,804, entitled “Methods of Fabricating Complex Two-Dimensional Conductive Silicides,” which is incorporated herein by reference in its entirety for the teachings therein.
Generally, various growth parameters, such as pressure, precursor ratios, temperatures and carrier gases, results in various silicide nano structures. In an embodiment, the 2D conductive silicide nanostructures are titanium silicide (TiSi2) nanonets. It should be noted that other 2D conductive silicide nanostructures can be fabricated using the methods of the presently disclosed embodiments, including, but not limited to, nickel silicide, iron silicide, platinum silicide, chromium silicide, cobalt silicide, molybdenum silicide and tantalum silicide. Methods of fabricating 2D conductive silicides include performing chemical vapor deposition, wherein one or more gas or liquid precursor materials carried by a carrier gas stream react to form a nanostructure having a mesh-like appearance and including a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle.
A CVD system used for the fabrication of complex two-dimensional (2D) conductive silicide nanostructures of the presently disclosed embodiments can have, for example, automatic flow and pressure controls. Flow of a precursor gas and a carrier gas are controlled by mass flow controllers, and fed to a growth (reaction) chamber at precise flow rates. The flow rate for the precursor gas is between about 20 standard cubic centimeters per minute (sccm) and about 100 sccm. In an embodiment, the flow rate for the precursor gas is about 50 sccm. In an embodiment, the precursor gas is present at a concentration ranging from about 1.3×10−6 mole/L to about 4.2×10−6 mole/L. In an embodiment, the precursor gas is present at a concentration of about 2.8±1×10−6 mole/L. The flow rate for the carrier gas is between about 80 standard cubic centimeters per minute (sccm) and about 130 sccm. In an embodiment, the flow rate for the carrier gas is about 100 sccm. A precursor liquid is stored in a cylinder and released to the carrier gas mass flow controller through a metered needle control valve. The flow rate for the precursor liquid is between about 1.2 sccm and 5 sccm. In an embodiment, the flow rate for the precursor liquid is about 2.5 sccm. In an embodiment, the precursor liquid is present at a concentration ranging from about 6.8×10−7 mole/L to about 3.2×10−6 mole/L. In an embodiment, the flow rate for the precursor liquid is present at a concentration of about 1.1±0.2×10−6 mole/L. All precursors are mixed in a pre-mixing chamber prior to entering the reaction chamber. The pressure in the reaction chamber is automatically controlled and maintained approximately constant by the combination of a pressure transducer and a throttle valve. In an embodiment, the system is kept at a constant pressure of about 5 Tarr during growth. The variation of the pressure during a typical growth is within 1% of a set point. All precursors are kept at room temperature before being introduced into the reaction chamber. A typical reaction lasts from about five minutes up to about twenty minutes. The reaction chamber is heated by a horizontal tubular furnace to temperature ranging from about 650° C. to about 685° C. In an embodiment, the reaction chamber is heated to a temperature of about 675° C.
In an embodiment, the precursor liquid is a titanium containing chemical. Examples of titanium containing chemicals include, but are not limited to, titanium beams from high temperature (or electromagnetically excited) metal targets, titanium tetrachloride (TiCl4), and titanium-containing organomettalic compounds. In an embodiment, the precursor gas is a silicon containing chemical. Examples of silicon containing chemicals include, but are not limited to, silane (SiH4), silicon tetrachloride (SiCl4), disilane (Si2H6), other silanes, and silicon beams by evaporation. In an embodiment, the carrier gas is selected from the group consisting of hydrogen (H), hydrochloric acid (HCl), hydrogen fluoride (HF), chlorine (Cl2), fluorine (F2), and an inert gas.
2D conductive TiSi2 nanostructures disclosed herein are spontaneously fabricated in the CVD system when the precursors react and/or decompose on a substrate in the growth chamber. This spontaneous fabrication occurs via a seedless growth, i.e., no growth seeds are necessary for the growth of the 2D conductive TiSi2 nanostructures. Therefore, impurities are not introduced into the resulting nanostructures. The fabrication method is simple, no complicated pre-treatments are necessary for the receiving substrates. The growth is not sensitive to surfaces (i.e., not substrate dependent). No inert chemical carriers are involved (the carrier gas also participates the reactions). 2D conductive TiSi2 nanostructures disclosed herein exhibit high conductivity and suitably high surface area.
High resolution transmission electron microscopy (HRTEM) images and electron diffraction (ED) patterns of different regions of the nanobelt 110 from
Complex core/shell hetero-nanostructures of the present disclosure, which combine highly conductive two-dimensional (2D) complex nanonets with a photoactive coating, offer outstanding charge transport among branches that are linked by single crystalline junctions. In an embodiment, the hetero-nanostructures of the present disclosure combine highly conductive complex TiSi2 nanonets (NNs) with photoactive Fe2O3 coating (as termed herein, Fe2O3/TiSi2 hetero-nanostructures). In an embodiment, fabrication of complex Fe2O3/TiSi2 hetero-nanostructures of the present disclosure includes the growth of two-dimensional (2D) TiSi2 NNs by reacting TiCl4 and SiH4 in H2 using CVD, as described above. In brief, 50 sccm SiH4 (10% in He), 2 sccm Cl4 and 100 sccm H2 are co-fed into the growth chamber simultaneously. The reaction typically takes place at 675° C. for about 15 minutes. The system is maintained at 5 Torr through out the growth, and growth occurs without growth seeds. Once produced, the SiH4 feeding is stopped while the TiCl4 and H2 flow are continued at 675° C. for about 5 minutes. Ti foils coated with 100 nm Pt film was used to collect the products. This treatment results in a thin Ti passivation layer that is important to the properties. The CVD system used to grow the highly conductive complex TiSi2 nanonets of the present disclosure have automatic pressure and flow controls.
In an embodiment, as illustrated in
After the annealing step, the hematite shell is synthesized on the conductive nanonets. In an embodiment, the iron oxide coating is synthesized by an ALD process using iron tert-butoxide (heated to about 140° C.) and water (at about 25° C.) as iron and oxygen precursor, respectively. In an embodiment, iron tert-butoxide is synthesized as follows: 6.3 g sodium tert-butoxide (Sigma) and 3.2 g iron chloride (anhydrous, Sigma) are mixed in 240 mL tetrahydrofuran (anhydrous, Sigma). The mixture is heated to 60° C. by water bath for 5 h. Afterward, the solvent is removed by distillation at 80° C. and then transferred to a precursor bubbler for the ALD growth. During the preparation, Ar is flowing to keep the reaction under inert gas environment. The ALD growth can be carried out at 180° C. with 10 sccm N2 flowing. TiSi2 nanonets and FTO substrate are used as substrate. In an embodiment, a stopvale mode procedure for the growth of iron oxide is employed to ensure the reaction between iron precursor and water. In an embodiment, the stopvalve mode procedure is as follows:
The stopvalve mode procedure described above yielded a much higher growth rate (0.6 Å/cycle) of iron oxide compared with what has been disclosed in the literature (the highest rate previously reported was 0.26 Å/cycle). Typically, a 400-cycle iron oxide growth produced a 25 nm thick film. After growth, the samples were postannealed in O2 for 15 min at 500° C. to improve crystallinity.
A Fe2O3/TiSi2 hetero-nanostructure of the present disclosure, produced using methods described above, was examined using a Scanning Electron Microscope and a Transmission Electron Microscope.
Previously, it has generally been accepted that iron oxide is not photoactive when thinner than 50 nm. Such a property will greatly limit its applications for water splitting. In an embodiment, the hetero-nanostructures of the present disclosure, having an iron oxide shell of less than 50 nm, are photoactive, as evidenced in the plots shown in
An X-ray Diffractrometer (XRD) and an X-ray photoelectron Spectrometer (XPS) was used for the crystal structure study and elemental analysis, respectively.
Once prepared, the Fe2O3/TiSi2 hetero-nanostructures (Fe2O3 thickness: 25 nm) were then made into electrodes. Ti foils coated with Fe2O3/TiSi2 hetero-nanostructures were connected to a copper wire using conductive silver epoxy (SPI supplies). Afterwards, the entire substrate except the front side with the hetero-nanostructures was covered by non-conductive Loctite® Hysol® epoxy. A UV-Ozone (Jelight Company Inc.) exposure (3 min) was performed to this region immediately before the PEC measurements. PEC measurements were conducted using a CHI 608C Potentiostat/Galvanostat in a three-electrode configuration, with Fe2O3/TiSi2 as working electrode, a Pt mesh as the counter electrode, and a Hg/HgO in 1M NaOH as the reference electrode. The electrolyte was 1 M NaOH solution, the pH of which was 13.60 as verified by an Orion 4-Star pH meter (Thermo Scientific). The measured voltage was converted into the potential vs. reversible hydrogen electrode (RHE). The current flowing into the photoanode was defined as positive. As a precaution to exclude any influence of dissolved gases such as O2, the solution was bubbled with N2 for 20 min before a measurement. In a typical experiment, the potential was linearly swept from 0.8 V to 1.7 V vs. RHE at a scan rate of 10 mV/s. Other sweeping ranges, directions and rates were also tested. The light source was an AM 1.5 solar simulator (Oriel, mode 96000) with the illumination intensity adjusted to 100 mW/cm2.
The absorbance was calculated from the formula A=−log(T+R),4 where A is the absorbance, T is the total transmittance, and R is the total reflectance. T and R was measured using integrating sphere (Sphere Optics) coupled with a spectrometer (Ocean Optics USB 4000). Iron oxide on quartz was used for this measurement to eliminate the influence of the FTO coating. The incident photon-to-charge conversion efficiencies (IPCE) were measured using a solar simulator (Oriel, mode 96000) coupled with a monochromator (Oriel Cornerstone 260). The intensity of the monochromatic light was measured by a calibrated Si detector (Oriel, Model 71640). The working electrode was biased at 1.53 V (vs. RHE) using the same configuration as described above. Absorbed photon-to-current conversion efficiencies (APCE) were calculated for iron oxide on FTO substrate using following equation:
where A is the absorbance as described above.
Electrochemical impedance spectroscopy measurement was performed by a three-electrode configuration using CHI 604C, as described above. A sinusoidal voltage perturbation, with amplitude of 5 mV and frequencies ranging from 100,000 to 1 Hz was superimposed on the bias voltage. The impedance was measured at bias voltages from 1.1 to 2.1 V vs RHE. All EIS measurements were performed in dark. The Nyquist plot obtained from EIS measurement was simulated using the following equivalent circuit and the CHI 604C software:
Equivalent circuit used to simulate the Nyquist plot measured by EIS. Rs is the series resistance. Rsc and Csc represent the charge transfer resistance and capacitance of space charge region, respectively. Rss and Css represent the resistance and capacitance of surface states, respectively. Rdl and CPE represent the resistance and capacitance of double layer, respectively.
The relatively low photocurrent of intrinsic iron oxide measured on planar FTO substrate is in part due to the poor light absorption by the thin film on FTO. To estimate the maximum photocurrent an electrode can deliver under solar AM 1.5 illumination, it was assumed that all photons are absorbed by the electrode and the absorbed photon-to-charge conversion efficiencies (APCE) were calculated. By integrating the APCE spectrum over the photon flux obtained from standard AM 1.5 solar spectrum, the maximum photocurrent expected from intrinsic iron oxide was obtained and found to be approximately 2 mA/cm2 at 1.53V vs RHE.
The incident photon-to-charge conversion efficiencies (IPCE) of the Fe2O3/TiSi2 hetero-nanostructure was measured as a function of wavelength, and the data are plotted in
The ability to prepare ultra-thin crystalline Fe2O3 allows for the measurement of the internal quantum efficiencies without being confounded by poor charge collection. The results reveal that even when only the absorbed photons are considered, a relatively low (<50%) quantum efficiency is measured, and the efficiency is especially low in the long wavelength range where the excited electrons are of lower energy (e.g., ˜16% at 500 nm), as shown in
Because a low-impedance across the interface between Fe2O3 and TiSi2 is desired in the realization of the nanonet-based design, a study was carried out on this interface using EIS in dark under steady-state conditions. A potential (varying from 1.1 to 2.1 V) was applied and the system was allowed to equilibrate for 5 min. Afterwards, an alternating current (AC) perturbation (frequencies changing from 100,000 to 1 Hz) to the applied potential with a magnitude of 5 mV was exerted, and the impedance change in response to the perturbation was measured. A typical set of data (at 1.9V) is plotted in
An equivalent electrical circuit was then employed to analyze the data. This technique allows one to single out two important elements of the hetero-nanostructures of the present disclosure in a quantitative fashion: the series resistance including that between TiSi2 and Fe2O3, as well as the capacitance of the depletion region within Fe2O3, as shown in
In an embodiment, to improve the collection of charges generated by long wavelength photons close to the bandgap edge so as to result in the reduction in charge recombination, doped iron oxide may be used as the photoactive shell in the hetero-nanostructures of the present disclosure. Doping has been studied to improve the photoelectrochemical performance of iron oxide photoanode by improving the charge transfer or by reducing charge recombination. To further improve the performance of iron oxide, the doping can be realized in a hetero-nanostructure of the present disclosure. Atomic layer deposition, which is used to deposit the iron oxide film, has the advantage of tuning the film composition with a high degree of control. Si, Ti, or Sn which are the most effective dopants, could be used. For example, tetrakis (dimethylamino)silane or vinyl-trimethoxysilane can be used as the silicon precursor. Titanium tetrachloride or titanium isopropoxide can be used as the titanium precursor. Tin tetrachloride could be used as the tin precursor. Dopant is incorporated during the ALD growth of iron oxide with tunable concentration. The dopant concentration could be tuned by adjusting the ratio of pulse cycles of iron and dopant precursor.
In an embodiment, to improve the collection of charges generated by long wavelength photons close to the bandgap edge so as to result in the reduction in charge recombination, co-catalysts may be added to iron oxide and the co-catalysts/iron oxide may be used as the photoactive shell in the hetero-nanostructures of the present disclosure. Oxygen evolving catalyst has been studied to improve the performance of iron oxide photoanode by reducing the oxygen generation overpotential. Various catalysts such as iridium oxide nanoparticles, cobalt-phosphate, or brudvig-crabtree catalyst can be used to improve the performance. These catalysts can be easily deposited via different methods on the electrodes. For example, the iridium oxide nanoparticles can be synthesized by a solution-based approach and then deposited on the electrode by a simple electrophoresis method. Cobalt-phosphate catalyst can be deposited via electrodeposition in a solution containing cobalt nitrate and potassium phosphate. A simple method via thermal treatment can be employed to deposit Mn-based catalyst derived from brudvig-crabtree catalyst. It is believed that by combining these various oxygen evolving catalysts with a hematite hetero-nanostructure of the present disclosure, the efficiency can be further improved.
In an embodiment, a hetero-nanostructure of the present disclosure includes a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle, the plurality of nanobeams including a conductive silicide core having an n-type photoactive hematite shell.
In an embodiment, a device for splitting water to generate hydrogen and oxygen includes a first compartment having a two-dimensional hetero-nanostructure, the hetero-nanostructure having a plurality of connected and spaced-apart nanobeams, each nanobeam substantially perpendicular to another nanobeam, the plurality of nanobeams including an n-type photoactive hematite shell having a conductive core; and a second compartment having a p-type material, wherein the first compartment and the second compartment are separated by a semi-permeable membrane.
In an embodiment, a method of fabricating a nanonet-based hematite hetero-nanostructure includes performing chemical vapor deposition so as to fabricate a two-dimensional conductive silicide nanostructure, wherein one or more gas or liquid precursor materials carried by a first carrier gas stream react to form the nanostructure, and wherein the nanostructure has a mesh-like appearance and includes a plurality of connected and spaced-apart nanobeams linked together at an about 90° angle; annealing the nanostructure; and performing atomic layer deposition so as to deposit a conformal crystalline hematite around the nanostructure, wherein the film ranges from about 10 nm to about 40 nm, and wherein one or more gas or liquid precursor materials carried by a second carrier gas stream react to form the hematite hetero-nanostructure. In an embodiment, the method further includes annealing the hematite hetero-nanostructure. In an embodiment, the conductive silicide is a titanium silicide. In an embodiment, the one or more gas or liquid precursor materials of the chemical vapor deposition is selected from a titanium containing chemical and a silicon containing chemical. In an embodiment, the carrier gas of the chemical vapor deposition is selected from the group consisting of H, HCl, HF, Cl2, and F2. In an embodiment, the one or more gas or liquid precursor materials of the atomic layer deposition is selected from a titanium containing chemical such as Ti(i-PrO)4.
All patents, patent applications, and published references cited herein are hereby incorporated by reference in their entirety. It will be appreciated that several of the above-disclosed and other features and functions, or alternatives thereof, may be desirably combined into many other different systems or applications. Various presently unforeseen or unanticipated alternatives, modifications, variations, or improvements therein may be subsequently made by those skilled in the art which are also intended to be encompassed by the following claims.
This application claims the benefit of and priority to U.S. Provisional Application Ser. No. 61/432,830, filed Jan. 14, 2011, the entirety of which is hereby incorporated herein by reference for the teachings therein.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2012/021230 | 1/13/2012 | WO | 00 | 9/19/2013 |
Number | Date | Country | |
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61432830 | Jan 2011 | US |