The present invention relates generally to the fabrication of semiconductor devices, and more particularly to a method of fabricating an oxide layer on a semiconductor device.
Semiconductor devices are typically fabricated by sequentially depositing insulating (or dielectric) layers, conductive layers and semiconductive layers of material over a semiconductor substrate, and patterning the various layers using lithography to form circuit components and elements thereon. One type of insulating layer commonly deposited on semiconductor devices is an oxide layer. Wet oxidation is widely used in the semiconductor industry for forming a high quality oxide film. Wet oxidation may be represented by Eq. 1:
Si+H2O→SiO2+H2 and Si+O2→SiO2. Eq. 1
However, wet oxidation is often undesirable for use in some applications because the oxidation rate is very slow, e.g., about 1-2 Å/min, which causes a decreased throughput of semiconductor devices in the fabrication process and increases costs. The deposition rate of wet oxidation is dependent on several parameters, such as reaction temperature, crystal orientation of the substrate, and ambient humidity, as examples.
Supercritical fluids or solutions are created when the temperature and pressure of a solution are above the critical temperature and pressure of the fluid. In a supercritical fluid, there is no differentiation between the liquid and gas phases, and the fluid comprises a dense gas in which the saturated vapor and saturated liquid states are identical. Near-supercritical fluids or solutions exist when the reduced temperature and pressure of a solution are both greater than about 0.8×(Tc, Pc), but the solution is not yet in the supercritical phase. Due to their high density, supercritical and near-supercritical fluids possess superior solvating properties.
Supercritical fluids have been used in thin film processing and other applications as developer reagents or extraction solvents. Murthy et al. (U.S. Pat. No. 4,737,384) describe a physical deposition method for depositing metals and polymers onto substrates by dissolving the metal or polymer in a solvent at supercritical temperature, and reducing the temperature and pressure to deposit the metals and polymer onto a substrate. Sievers et al. (U.S. Pat. No. 4,970,093) teach a chemical vapor deposition method (CVD) in which a supercritical fluid is used to dissolve a precursor, the solution is rapidly expanded, and a chemical reaction is induced in the supercritical solution near a substrate surface to deposit a film by CVD. Watkins et al. (U.S. Pat. No. 5,789,027) describe a method termed Chemical Fluid Deposition (CFD) for depositing a material onto a substrate surface, in which a supercritical fluid is used to dissolve a precursor of the material to be deposited, a substrate is exposed to the solution, and a reaction reagent is introduced that initiates a chemical reaction involving the precursor, thereby depositing the material onto the substrate.
Although the prior art methods described above take advantage of the unique properties of supercritical fluids, the utility of supercritical fluids in semiconductor fabrication has only begun to be realized.
Embodiments of the present invention achieve technical advantages by using a supercritical fluid to form a layer of oxide on a surface of a semiconductor device. An oxidizing agent is mixed with a fluid such as water in a supercritical or near-supercritical state, and a substrate or workpiece is exposed to the mixture to form an oxide layer on exposed surfaces of the workpiece. In one embodiment, the method includes introducing nitrogen into the oxide film.
In accordance with a preferred embodiment of the present invention, a method of forming an oxide layer includes providing a workpiece and providing a fluid, the fluid having a temperature and a pressure. The temperature and pressure of the fluid are increased until the fluid reaches a supercritical or near-supercritical state. At least one oxidizing agent is provided, and the supercritical or near-supercritical state fluid is combined with the at least one oxidizing agent to form a supercritical or near-supercritical state mixture. The supercritical or near-supercritical state mixture is applied on the workpiece to form an oxide layer on the workpiece.
In accordance with another preferred embodiment of the present invention, a method of forming an oxide layer includes providing a workpiece, and exposing the workpiece to a mixture of a supercritical state fluid or near-supercritical state fluid and at least one oxidizing agent, forming a layer of oxide on the workpiece.
In accordance with yet another preferred embodiment of the present invention, a method of forming an oxide layer includes providing a workpiece, the workpiece having a surface, combining water in a supercritical state with an oxidizing agent, and exposing the workpiece to the combined supercritical water and oxidizing agent, forming an oxide layer on the surface of the workpiece.
Advantages of preferred embodiments of the present invention include removing surface contaminations and forming an oxide film simultaneously. Nitrogen can be introduced to dope nitrogen into the oxide film formed, in one embodiment. Oxide films may be formed at a faster rate than prior art oxide formation methods. Embodiments of the invention result in semiconductor devices having high quality and density oxide layers, and increased throughput.
The foregoing has outlined rather broadly the features and technical advantages of embodiments of the present invention in order that the detailed description of the invention that follows may be better understood. Additional features and advantages of embodiments of the invention will be described hereinafter, which form the subject of the claims of the invention. It should be appreciated by those skilled in the art that the conception and specific embodiments disclosed may be readily utilized as a basis for modifying or designing other structures or processes for carrying out the same purposes of the present invention. It should also be realized by those skilled in the art that such equivalent constructions do not depart from the spirit and scope of the invention as set forth in the appended claims.
For a more complete understanding of embodiments of the present invention and the advantages thereof, reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which:
Corresponding numerals and symbols in the different figures generally refer to corresponding parts unless otherwise indicated. The figures are drawn to clearly illustrate the relevant aspects of the preferred embodiments and are not necessarily drawn to scale.
The making and using of the presently preferred embodiments are discussed in detail below. It should be appreciated, however, that the present invention provides many applicable inventive concepts that can be embodied in a wide variety of specific contexts. The specific embodiments discussed are merely illustrative of specific ways to make and use the invention, and do not limit the scope of the invention.
The present invention will be described with respect to preferred embodiments in a specific context, namely in semiconductor device fabrication. The invention may also be applied, however, to other applications where the formation of an oxide layer is required.
With reference now to
The coordinates (Tc, Pc) define a critical point where the temperature and pressure are equal to the critical temperature Tc and critical pressure Pc, respectively. A region where the temperature and pressure are equal to or higher than the critical temperature Tc and critical pressure Pc, respectively, is defined as a supercritical region Rcp. In the supercritical region Rcp, the fluid is defined to be in a supercritical state. A region where the temperature is equal to or higher than the critical temperature Tc but the pressure is slightly lower than the critical pressure Pc, and a region where the pressure is equal to or higher than the critical pressure Pc but the temperature is slightly lower than the critical temperature Tc, are defined as near-supercritical regions Rpcp. When the material is in the supercritical region Rcp, the material exhibits different properties than when the material is in the gas, liquid or solid phases.
Next, a technique of forming an oxide layer in a supercritical or near-supercritical fluid combined with an oxidizing agent will be described in accordance with an embodiment of the present invention.
In accordance with embodiments of the present invention, a fluid in a supercritical or near-supercritical state is supplied from the cylinder 50. The fluid may comprise water or CO2, as examples, although other fluids may alternatively be used. The temperature/pressure regulator 51 is adapted to control the temperature and pressure of the fluid to be supplied in such a manner as to make the fluid enter the supercritical or near-supercritical state. The oxidant concentration controller 52 is adapted to control the concentration of the one or more oxidants, which are supplied from the oxidant feeder 53 as oxidizing agents for the oxide layer 12 that will be formed on the workpiece 10. The temperature/pressure regulator 51 may be connected to the cylinder 50 via a pipe. The controller 51 is adapted to control the temperature and pressure of the supercritical fluid.
The fluid in a preferred embodiment comprises H2O that is held in the supercritical state or region Rcp of
In another embodiment, the fluid comprises H2O that is held in near-supercritical regions Rpcp (of
The fluid that is combined with an oxidizing agent in accordance with embodiments of the present invention to form an oxide layer may alternatively comprise CO2 or other fluids, for example. Preferably, in one embodiment, the temperature of heating the fluid to supercritical near-supercritical conditions is about 300° C. to about 750° C., and the pressure of pressurizing the fluid to supercritical or near-supercritical conditions is about 176 to about 440 bar, as examples, although alternatively, other temperatures and pressures may be used.
The oxidant feeder 53 includes at least one container. Each container is adapted to store oxidizing agents for the oxide layer 12 to be formed on the workpiece 10. In accordance with an embodiment of the invention, the oxide layer 12 is formed by exposing the workpiece 10 to an oxidant (also referred to herein as an oxidizing agent) combined with a supercritical fluid or near-supercritical fluid. The oxidizing agent in accordance with one embodiment of the present invention comprises O1, O3, or H2O2, which have a strong oxidation capability. In another embodiment, the oxidizing agent comprises a nitrogen-containing substance, such as N2O, NO2, N2O2, or NO as examples. The oxidizing agent may alternatively comprise other oxidants, and may comprise combinations of O2, O3, H2O2, N2O, NO2, N2O2, NO, and other oxidants, for example.
In another embodiment, the oxidizing agent may include other oxidants that have strong oxidation capability at high temperature and pressure, such as organic alcohol (e.g., CHOH, C2H5OH), organic acid (e.g., HCOOH, CH3COOH), or organic aldehyde (e.g., HCHO, CH3CHO), as examples. If these chemistries are added to the supercritical or near-supercritical fluid, then an even higher quality oxide layer 12 may be formed on a workpiece 10, depending on the temperature or pressure.
The oxidant concentration controller 52 is connected to the temperature/pressure regulator 51 and the oxidant feeder 53 via respective pipes. The oxidant concentration controller 52 is adapted to mix the oxidizing agents as respective solutes, for example, in supercritical water. The oxidant concentration controller 52 is also adapted to control the concentration of the solutes at predetermined concentrations and supply the mixture to the vessel 17.
In accordance with an embodiment of the invention, the formation of the oxide layer 12 and removal of any contaminants from the workpiece surface are carried out simultaneously. This may be achieved in the following manner. First, the oxidant concentration controller 52 adjusts the mixture ratio of supercritical water that has been supplied from the temperature/pressure regulator 51 and the oxidants that have been supplied from the oxidant feeder 53. In one illustrative embodiment, the concentrations of the oxidizing agent in supercritical water are all controlled at about 10% by volume. The flow rate of the supercritical state mixture of the water and oxidizing agents on the workpiece may comprise about 0.1 liter per minute to about 25 liters per minute, for example.
In the vessel 17, the temperature of the workpiece may be controlled by the sample stage 18, e.g., at about 650° C., and the mixture of supercritical water and oxidant that has been supplied from the oxidant concentration controller 52 is applied on the surface of the workpiece 10, thereby forming an oxide layer 12. Again, preferably in one embodiment, surface contaminations are removed simultaneously with the formation of the oxide layer 12. The removal of surface contaminations may be accomplished by organic compound oxidation and decomposition, for example.
The workpiece 10 is then placed within a reaction vessel 17 such as the one shown in
The oxide layer 12 may be comprised of an oxide, oxynitride or any combination thereof including multilayers. In one preferred embodiment, the oxide layer 12 comprises an oxynitride. A nitrogen-doped gate oxide may be particularly advantageous in certain applications, for example. When an oxynitride is employed as the oxide layer 12, the oxide layer 12 may be formed in the presence of any oxygen/nitrogen-containing oxidant, which may be mixed with supercritical water, for example. Suitable oxygen/nitrogen-containing oxidants include, but are not limited to: NO, NO2, N2O2, N2O and combinations thereof, for example. In one preferred embodiment, the oxide layer 12 is formed in an oxygen/nitrogen-containing ambient that comprises from about 10% to 50% NO which is admixed in supercritical water. The flow rate of the supercritical state mixture of the water and oxidizing agents on the workpiece may comprise about 0.1 liter per minute to about 25 liters per minute, for example.
The thickness of the oxide layer 12 formed utilizing embodiments of the present may comprise a thickness of from about 100 to about 400 nm, for example, although alternatively, the oxide layer 12 thickness may comprise other thicknesses. Preferably the oxide layer 12 is formed faster than prior art wet deposition techniques. For example, the oxide layer 12 is formed at a rate of about 5 Angstroms per minute or greater in a preferred embodiment.
A subsequent material 14, which may comprise a gate material or gate conductor, as examples, may then be formed on the oxide layer 12, as shown in
After forming material 14 on the oxide layer 12, the workpiece 10 may then be patterned utilizing conventional processing steps well known in the art which are capable of forming the patterned structure shown in
In another embodiment of the present invention, as shown in
The workpiece 20 is exposed to a mixture of a supercritical state fluid such as water and an oxidizing agent such as O2, O3, H2O2, N2O, NO2, N2O2, NO, CHOH, C2H5OH, HCOOH, CH3COOH, HCHO, CH3CHO, other oxidants, or combinations thereof, as examples, as described above, to form capacitor dielectric 36, for example. The capacitor dielectric 36 may be comprised of an oxide, oxynitride or any combination thereof, including multilayers thereof. The thickness of the capacitor dielectric 36 may comprise about 100 to about 400 nm, and may alternatively comprise other thicknesses, for example.
A second layer of metal 38 is then deposited over the layer of capacitor dielectric 36. The second layer of metal 38 is polished down to the surface of the layer of capacitive dielectric 36. The surface of the polished second layer of metal 38 is in a plane with the surface of the layer of capacitor dielectric 36 where the layer of capacitor dielectric 36 overlays the second layer of dielectric 26, for example. The MIM capacitor includes a top plate 38, capacitor dielectric 36 formed utilizing embodiments of the present invention, and a bottom plate 32, as shown.
The method of forming an oxide layer described herein is particularly advantageous when used to oxidize high dielectric constant (K) materials disposed over the surface of a workpiece, such as Hf/Zr, Si/Al, Ti/Sr, Y/Ba, or La/Ta, as examples.
When the fluid combined with the oxidizing agent described herein comprises supercritical water, this is advantageous for several reasons. Because supercritical water has a high O2 solubility, the oxidation rate is increased. The high humidity of supercritical water also contributes to an increased oxidation rate, as shown by Eq. 2 and Eq. 3:
Si+H2O→SiO2+H2 Eq. 2
Si+O2→SiO2 Eq. 3
Furthermore, the low polarity of supercritical water results in increased organic solubility, as shown in Eq. 4:
CxHy(s)→CxHy(g)+O2→CO2+H2O Eq. 4
In addition, because supercritical water has a low surface tension, high aspect ratio features are filled completely rather than having void formation in lower regions of the high aspect ratio structures. Because the supercritical water oxidizes and cleans the workpiece surface simultaneously, reduced cost and improved performance are achieved.
Advantages of embodiments of the invention include providing a novel method of forming an oxide layer that decreases the oxide formation time and provides a high quality oxide layer. Nitrogen can be introduced during the oxide formation, forming an oxynitride layer on the workpiece. Increased throughput of semiconductor device fabrication can be achieved in accordance with embodiments of the present invention. The surface of a workpiece is advantageously cleaned of contaminants simultaneously with the formation of the oxide layer, in accordance with embodiments of the invention.
Although embodiments of the present invention and their advantages have been described in detail, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention as defined by the appended claims. For example, it will be readily understood by those skilled in the art that many of the features, functions, processes, and materials described herein may be varied while remaining within the scope of the present invention. While embodiments of the present invention are described herein in the formation of a gate oxide layer of a FET (
Moreover, the scope of the present application is not intended to be limited to the particular embodiments of the process, machine, manufacture, composition of matter, means, methods and steps described in the specification. As one of ordinary skill in the art will readily appreciate from the disclosure of the present invention, processes, machines, manufacture, compositions of matter, means, methods, or steps, presently existing or later to be developed, that perform substantially the same function or achieve substantially the same result as the corresponding embodiments described herein may be utilized according to the present invention. Accordingly, the appended claims are intended to include within their scope such processes, machines, manufacture, compositions of matter, means, methods, or steps.
This application claims the benefit of U.S. Provisional Application No. 60/529,525, filed on Dec. 15, 2003, entitled “Method of Forming an Oxide Layer Using a Mixture of a Supercritical State Fluid and an Oxidizing Agent,” which application is hereby incorporated herein by reference.
Number | Date | Country | |
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60529525 | Dec 2003 | US |