1. Field of the Invention
Embodiments of the invention generally relate to methods for depositing materials on substrates, and more specifically to methods of forming metal interconnects.
2. Description of the Related Art
Multilevel, 45 nm node metallization is one of the key technologies for the next generation of very large scale integration (VLSI). The multilevel interconnects that lie at the heart of this technology possess high aspect ratio features, including contacts, vias, lines and other apertures. Reliable formation of these features is very important for the success of VLSI and the continued effort to increase quality and circuit density on individual substrates. Therefore, there is a great amount of ongoing effort being directed to the formation of void-free features having high aspect ratios of 10:1 (height:width) or greater.
Tungsten is a choice metal for filling VLSI features, such as sub-micron high aspect ratio contact (HARC) on a substrate. Contacts are formed by depositing a conductive interconnect material, such as tungsten into an aperture (e.g., via) on the surface of insulating material disposed between two spaced-apart conductive layers. A high aspect ratio of such an opening may inhibit deposition of a conductive interconnect material to fill an aperture. Although tungsten is a popular interconnect material, vapor deposition processes for depositing tungsten may suffer by forming a void or a seam within the contact plug, as illustrated in
Defects, such as a seam or a void 114, may cause a series of problems during the fabrication of electronic devices depicted herein. The resistance to current flow through the plug 103 is impaired due to the lack of tungsten material in the void 114. However, a more serious obstacle during fabrication is the displacement of voids from one layer to the next. For example, subsequent fabrication processes of substrate 100 may include the deposition of layer 120 (e.g., dielectric layer) on conductive layer 112. During subsequent thermal processing, such as an annealing process, the material 116 from conductive layer 112 may diffuse into void 114 and form a void 118 within conductive layer 112. As illustrated in
Therefore, a need exists for a method to form an interconnect on a contact plug that is free of voids. If a void is present, then selected materials are deposited to cap or fill the voids and prevent subsequent displacement of conductive layers deposited thereon.
The present invention generally provide a method of forming an electrical contact on a silicon substrate, comprising providing a substrate containing an exposed tungsten-containing contact plug exposed that has an exposed gap formed therein, exposing the substrate to a pretreatment process, wherein the pretreatment process is adapted to remove an oxide layer from a surface of the exposed tungsten-containing contact plug, filling the exposed gap with a fill material.
Embodiments of the invention further provide a method of forming an electrical contact on a silicon substrate, comprising providing a silicon substrate having a first dielectric layer which is disposed on a surface of the silicon substrate and a first aperture formed in the first dielectric layer, wherein a doped silicon containing region of the silicon substrate is exposed at the bottom of the first aperture, filling the first aperture formed in the first dielectric layer with a tungsten containing layer, wherein the tungsten containing layer is in electrical communication with the doped silicon containing region, removing an amount of the tungsten containing layer disposed on the first dielectric layer, wherein a gap formed in the tungsten containing layer during the step of filling the first aperture is exposed, and depositing a material on the surface of the silicon substrate to substantially cover the gap formed in the tungsten containing layer.
Embodiments of the invention further provide a method of forming an electrical contact on a silicon substrate, comprising providing a substrate containing first dielectric layer that contains at least one tungsten-containing contact plug that has an exposed surface, forming a second dielectric layer over the first dielectric layer and the tungsten-containing contact plug, forming a second aperture in the second dielectric layer that is in communication with the exposed surface of the tungsten-containing contact plug, and selectively filling the second aperture with a fill material.
Embodiments of the invention further provide a method of forming an interconnect on a silicon substrate, comprising providing a substrate having an aperture formed in a dielectric layer disposed on a surface of the substrate, wherein the aperture is in communication with an exposed surface of a tungsten-containing contact plug, dispensing a clean solution on an the exposed surface of the tungsten-containing contact plug, wherein the clean solution comprises hydrogen fluoride, disposing a preparation solution on the exposed surface of the tungsten-containing contact plug, wherein the preparation solution comprises a tungstate source, depositing a initiation layer on the exposed surface of the tungsten-containing contact plug using an activation solution, activating the initiation layer using a rinse activation solution, and selectively filling the second aperture with a fill material.
So that the manner in which the above recited features of the invention are attained and can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to the embodiments thereof which are illustrated in the appended drawings. It is to be noted, however, that the appended drawings illustrate only typical embodiments of this invention and are therefore not to be considered limiting of its scope, for the invention may admit to other equally effective embodiments.
Embodiments of the invention provide methods of forming a device over a tungsten-containing contact plug. In one aspect, a process of capping and filling defects formed in a tungsten-containing contact plug that have been exposed during a subsequent chemical mechanical polishing (CMP) process is performed. Defects that are present in the tungsten-containing contact plug may include gaps, voids, and/or seams (hereafter gaps). In one embodiment, gaps are plugged or capped with a material that will be able to withstand subsequent thermal processing and inhibit displacement of the formed void therein. Gaps may be filled, or plugged, by employing selective deposition process that include chemical vapor deposition (CVD), atomic layer deposition (ALD), and electroless deposition processes. Preferably, the material used to fill the gaps or voids may include nickel, cobalt, tungsten and alloys thereof. In another embodiment, the method may include the steps of pretreating and then subsequently filling the gap by use of a CVD, ALD or electroless process using a conductive material such as nickel, ruthenium, cobalt, tungsten and alloys thereof.
In an alternative embodiment, a gap may be filled with a dielectric material. In one example, a spin-on-glass (SOG) is deposited by a spin coating process. SOG materials typically include silicon dioxide (SiO2) or doped SiO2 materials. In another example, hafnium silicate is deposited by a vapor deposition process.
In another embodiment, the gaps within a tungsten plug are filled during a later process. For example, the gap is temporally ignored, a dielectric layer is deposited on the substrate surface covering the gap and a second aperture is formed therein by an etching process over the tungsten plug and revealing the gap. A barrier layer (e.g., tantalum-containing) and a seed layer (e.g., copper) are sequential deposited by vapor deposition processes, such as physical vapor deposition (PVD) process.
Capping Process
Gaps within a tungsten-containing contact plug may be filled with a material that will be stable during subsequent semiconductor fabrication processes and inhibit the creation voids in the subsequent deposited metal layers. Gaps may be capped by employing selective vapor deposition processes (e.g., CVD or ALD) or liquid deposition processes (e.g., electroless) to deposit a capping material, such as nickel, cobalt, tungsten and alloys thereof.
Dielectric layer 204 may contain a semiconductor material that includes silicon or silicon-containing materials. Dielectric layer 204 may be an insulating material such as silicon dioxide, silicon nitride, silicon-on-insulator (SOI), silicon oxynitride and/or carbon-doped silicon oxides, such as SiOxCy, for example, BLACK DIAMOND™ low-k dielectric, available from Applied Materials, Inc., located in Santa Clara, Calif. Contact layer 202 may contain a doped silicon layer. Tungsten layer 206 may contain tungsten, tungsten alloys or a tungsten-containing material that includes tungsten and oxygen, nitrogen, boron, silicon or combinations thereof. Due to the exposure to the atmospheric environment, the surface of the tungsten layer 206 may contain contaminates or oxides thereon.
Conductive layer 212 is deposited on the surface of substrate 200 containing capping layer 230 and dielectric layer 204, as depicted in
In other embodiments, substrate 200 may contain additional layers of material depending on the overall architecture of the electronic device. For example, dielectric layer 204 may contain a barrier layer (not shown) thereon prior to the deposition of conductive layer 212 and/or conductive layer 212 may also contain a barrier layer (not shown) thereon prior to the deposition of layer 220.
In one aspect, a CMP process may be performed on the substrate 200 to planarize the dielectric layer 204, capping layer 230 and tungsten layer 206. A planar surface may improve the device performance and reduce device to device variability due to the reduction in thickness variation of the conductive layer 212 near the capping layer 230, if the conductive layer 212 and capping layer 230 are formed from different materials.
A capping layer 230 containing a cobalt-tungsten alloy or a nickel-containing material may be deposited by an electroless process that utilizes either a pre-mixed solution or an in-line mixing process that combines solution components to generate the electroless solution. In one example, an electroless solution used to deposit a cobalt-tungsten alloy may contain a cobalt source, a tungsten source, a citrate source, a hypophosphite source, a borane reductant and other additives. In another example, an electroless solution used to deposit a nickel-containing material may contain a nickel source, a citrate source, a borane reductant and other complexing agents and additives. Other electroless deposition solutions and processes useful for depositing cobalt-tungsten alloys are further described in the commonly assigned U.S. patent application Ser. No. 10/967,919, entitled, “Selective Self-initiating Electroless Capping of Copper with Cobalt-containing Alloys,” filed on Oct. 18, 2004, which is incorporated by reference to the extent not inconsistent with the claimed aspects and description herein. Examples of cobalt-tungsten alloys that may electrolessly deposited include, but are not limited to cobalt boride (CoB), cobalt phosphide (CoP), cobalt tungsten phosphide (CoWP), cobalt tungsten boride (CoWB), cobalt molybdenum phosphide (CoMoP), cobalt molybdenum boride (CoMoB), cobalt rhenium boride (CoReB), cobalt rhenium phosphide (CoReP), derivatives thereof, or combinations thereof. Examples of nickel alloys that may electrolessly deposited include, but are not limited to nickel boride (NiB), nickel phosphide (NiP), nickel tungsten phosphide (NiWP), nickel tungsten boride (NiWB), nickel molybdenum phosphide (NiMoB), nickel molybdenum phosphide (NiMoP), nickel rhenium phosphide (NiReP), nickel rhenium boride (NiReB), derivatives thereof, or combinations thereof. In one aspect, the capping layer 230 preferably has a resistivity below about 10 microohm-cm and thus will have a resistivity similar to the material deposited in the tungsten layer 206. The resistance (R) of a circuit is equal to the resistivity (ρ) of the conductive material through which the current passes times the length (L) of the feature divided by the cross-sectional area (A) of the circuit through which the current passes (i.e., R=ρ(L/A)). Therefore, the addition of a capping layer 230 that is conductive, preferably metallic, will reduce the resistance of the circuit that utilizes the plug 203 (i.e., increase the effective cross-sectional area of the plug 203).
Filling Process
In an alternative embodiment, to fill a gap formed within a tungsten-containing contact plug, the gap may be pretreated and filled with a material prior to depositing a conductive layer thereon (e.g., element 350 in
A plasma pretreatment process is conducted for a predetermined time to reduce tungsten oxide surface 312 and form a metallic tungsten-containing surface 314. A plasma pretreatment process may occur for about 5 minutes or less, preferably in a range from about 1 second to about 60 seconds, more preferably from about 5 seconds to about 30 seconds. During the pretreatment process, the substrate is maintained at a temperature in a range from about 20° C. to about 150° C., preferably from about 50° C. to about 100° C. The process chamber is maintained at a pressure in a range from about 0.1 Torr to about 750 Torr, preferably from about 1 Torr to about 100 Torr, and more preferably from about 10 Torr to about 30 Torr.
The plasma treatment process may be conducted in a process chamber capable of plasma vapor deposition techniques. For example, the substrate may be placed into a plasma enhanced ALD (PE-ALD), a plasma enhanced CVD (PE-CVD) or high density plasma CVD (HDP-CVD) chamber, such as the ULTIMA HDP-CVD™, available from Applied Materials Inc., located in Santa Clara, Calif. An inductively coupled plasma generating device, capacitively coupled plasma generating device, or combination thereof may be used in a plasma chamber to carryout the plasma treatment process. During processing the tungsten oxide surface 312 is exposed to a reducing plasma containing a reductant to form the metallic tungsten-containing surface 314. The reductant may be diluted in a carrier gas and include hydrogen, diborane, silane, disilane, phosphine, derivatives thereof and combinations thereof. In one aspect, a carrier gas is delivered to the process chamber during the plasma pretreatment process. Carrier gases may be selected so as to also act as a purge gas for the removal of volatile reactants and/or by-products from the process chamber. Carrier gases or purge gases include helium, argon, hydrogen, forming gas and combinations thereof. The carrier gas may be provided at a flow rate in a range from about 100 sccm to about 5,000 sccm, preferably from about 500 sccm to about 2,500 sccm. The reductant may be provided at a flow rate in a range from about 5 sccm to about 500 sccm, preferably from about 10 sccm to about 100 sccm. The plasma may be formed using an RF power delivered to the plasma generating devices (e.g., showerhead in a capacitively coupled chamber or a substrate support) utilized in the plasma chamber where the RF power ranges from 100 W to 10,000 W at an RF frequency between about 0.4 kHz and about 10 GHz. In one aspect, the plasma is formed using a showerhead RF power setting and a substrate support RF power setting that is in a range from about 500 W to about 5,000 W at a frequency of about 13.56 MHz.
In an exemplary plasma pretreatment process, a substrate containing tungsten oxide is heated to about 50° C. and the process chamber is maintained at a pressure of about 10 Torr. A reducing plasma is exposed to the substrate containing hydrogen at a flow rate of about 1,000 sccm. The substrate is exposed to the reducing plasma for about 30 seconds to form a treated and reduced tungsten-containing layer.
In another exemplary plasma pretreatment process, a substrate containing tungsten oxide is heated to about 50° C. and the process chamber is maintained at a pressure of about 10 Torr. A reducing plasma is exposed to the substrate at a flow rate of about 500 sccm, whereas the reducing plasma contains diborane at a flow rate of about 50 sccm and a helium carrier gas at the flow rate of about 450 sccm. The substrate is exposed to the reducing plasma for about 30 seconds to form a treated and reduced tungsten-containing layer.
In another embodiment, the tungsten oxide surface 312 is exposed to a reducing vapor to form metallic tungsten-containing surface 314 to perform a vapor deposition process type pretreatment process. The reductant may include borane, diborane, borane-alkylsulfides, such as borane-dimethylsulfide (BH3.(CH3)2S), alkyboranes (e.g., ethylborane), phosphine, alkylposphines (e.g., dimethylphosphine), silane, disilane, trisilane, alkylsilanes (e.g., methylsilane), ammonia, hydrazine, hydrogen, derivatives thereof or combinations thereof. Preferably, the reductant is diborane, phosphine, silane, hydrazine, hydrogen or combinations thereof. In one aspect of the pretreatment process, the tungsten oxide surface 312 is exposed to a reducing vapor process for a predetermined time to form metallic tungsten-containing surface 314. The reducing vapor process may occur for about 5 minutes or less, preferably in a range from about 1 second to about 120 seconds, more preferably from about 5 seconds to about 90 seconds. During the reducing vapor process, the substrate is maintained at a temperature in a range from about 20° C. to about 150° C., preferably from about 50° C. to about 100° C. The process chamber is maintained at a pressure in a range from about 0.1 Torr to about 750 Torr, preferably from about 1 Torr to about 100 Torr, and more preferably from about 10 Torr to about 30 Torr. In one aspect, a reductant may be exposed to tungsten oxide surface 312 directly or diluted in a carrier gas. During the reducing vapor process, a carrier gas flow is established within the process chamber and exposed to the substrate. Carrier gases may be selected so as to also act as a purge gas for the removal of volatile reactants and/or by-products from the process chamber. Carrier gases or purge gases include helium, argon, nitrogen, hydrogen, forming gas and combinations thereof. The carrier gas may be provided at a flow rate in a range from about 100 sccm to about 5,000 sccm, preferably from about 500 sccm to about 2,500 sccm. The reductant may be provided at a flow rate in a range from about 5 sccm to about 500 sccm, preferably from about 10 sccm to about 100 sccm.
The reducing vapor process may be conducted in a process chamber capable of vapor deposition, such as an ALD process chamber or a CVD process chamber. A process chamber useful for ALD during the reducing vapor process is described in commonly assigned U.S. Pat. Nos. 6,916,398 and 6,878,206, which are both incorporated herein by reference.
In another embodiment of the pretreatment process, the tungsten oxide surface 312 is exposed to wet clean process to further oxidize and remove tungstate ion while leaving behind a metallic tungsten-containing surface 314. During a typical wet clean process a wet clean solution is dispensed across or sprayed on the surface of substrate 300. The wet clean process may be an in situ process performed in the same processing cell as a subsequent electroless deposition process. Alternatively, substrate 300 may be wet cleaned in a separate processing cell from the subsequent electroless deposition processing cell. The wet clean process usually includes an acidic wet clean solution with a pH of about 4 or less, preferably, in a range from about 1.5 to about 3. The tungsten oxide surface 312 typically requires an aggressive cleaning at low pH values. The pH of the wet clean solution is usually adjusted by adding an acid or a base to the predetermined value. The acid may include hydrochloric acid (HCl), hydrogen fluoride (HF), sulfuric acid (H2SO4), nitric acid (HNO3), phosphoric acid (HPO4), derivatives thereof and combinations thereof. The base may include a hydroxide salt, ammonia or an amine, such as diethanolamine (DEA), triethanolamine (TEA), derivatives thereof, salts thereof and combinations thereof. The wet clean solution also contains at least one chelator or complexing agent, such as a carboxylic acid or carboxylate, for example, a citrate, oxalic acid, glycine, salts thereof and combinations thereof. In one example, the wet clean solution contains about 0.05 M to about 0.5 M of citric acid and optionally up to about 0.25 M of methanesulfonic acid.
In one embodiment, the pretreatment process is used to etch and remove a portion of the tungsten oxide surface 312 to increase the size of the gap 310 in an effort to improve the ability of the subsequent deposition process steps (discussed below) to access and fill the gap 310. In one aspect, the process of increasing the gap 310 is performed using a wet clean process for a desired period of time.
Once tungsten oxide surface 312 is removed or reduced to reveal metallic tungsten-containing surface 314 by the processes described herein, a fill material 320 may be deposited thereon to fill the gap 310, as illustrated in
Next a conductive layer 350 is deposited onto substrate 300 to form a plug 321 (or via) that is in electrical contact with plug 303. Conductive layer 350 may contain copper, tungsten, aluminum or an alloy thereof. Preferably, conductive layer 350 contains copper or a copper alloy. Conductive layer 350 may be deposited by a vapor deposition process (e.g., CVD or PVD) or a liquid deposition process (e.g., electroless or electroplating).
In one aspect, a CMP process may be performed on the substrate 300 to planarize the dielectric layer 304, capping layer 330 and tungsten layer 306. A planar surface may improve the device performance and reduce device to device variability.
In one aspect, a fill material 320 containing a cobalt-tungsten alloy or nickel alloy may be deposited by an electroless process that exposes the substrate to an electroless solution within a process chamber. An example of an electroless solution for depositing a cobalt-tungsten alloy may contain a cobalt source, a tungsten source, a citrate source, a hypophosphite source, a borane reductant and other additives. Examples of cobalt-tungsten alloys that may electrolessly deposited include, but are not limited to cobalt boride (CoB), cobalt phosphide (CoP), cobalt tungsten phosphide (CoWP), cobalt tungsten boride (CoWB), cobalt molybdenum phosphide (CoMoP), cobalt molybdenum boride (CoMoB), cobalt rhenium boride (CoReB), cobalt rhenium phosphide (CoReP), derivatives thereof, or combinations thereof. Examples of nickel alloys that may electrolessly deposited include, but are not limited to nickel boride (NiB), nickel phosphide (NiP), nickel tungsten phosphide (NiWP), nickel tungsten boride (NiWB), nickel molybdenum phosphide (NiMoB), nickel molybdenum phosphide (NiMoP), nickel rhenium phosphide (NiReP), nickel rhenium boride (NiReB), derivatives thereof, or combinations thereof. Other electroless deposition solutions for cobalt-tungsten alloys are further described in the commonly assigned U.S. patent application Ser. No. 10/967,919, entitled, “Selective Self-initiating Electroless Capping of Copper with Cobalt-containing Alloys,” filed on Oct. 18, 2004, which is incorporated by reference to the extent not inconsistent with the claimed aspects and description herein. In another example, an electroless solution to deposit a nickel-containing material may contain a nickel source, a citrate source, a borane reductant and other complexing agents and additives. An exemplary electroless deposition process cell that may be one or more of the electroless deposition processes described herein is further described in the commonly assigned and copending U.S. patent application Ser. No. 10/996,342, filed Nov. 22, 2004 and U.S. patent application Ser. No. 11/175,251, filed Jul. 6, 2005, which are both incorporated by reference in their entirety.
In one aspect, the fill material 320 preferably has a resistivity below about 10 microohm-cm and thus will have a resistivity similar to the material deposited in the tungsten layer 306. The resistance (R) of a circuit is equal to the resistivity (p) of the conductive material through which the current passes times the length (L) of the feature divided by the cross-sectional area (A) of the circuit through which the current passes (i.e., R=ρ(L/A)). Therefore, the addition of a fill material 320 that is conductive, preferably metallic, will reduce the resistance of the circuit that utilizes the plug 303 (i.e., increase the effective cross-sectional area of the plug 303) and thus improve the device performance and reliability (e.g., reduces resistive heating effects).
Ruthenium Containing Layer Deposition Process Sequence
In an alternative embodiment,
Ruthenium tetroxide may be delivered to the substrate in a vapor deposition process, such as an ozone generation process, or in a liquid deposition process, such as an aqueous solution or suspension. Preferably, ruthenium tetroxide is generated by exposing a ruthenium-containing source to an oxidizing gas. Ruthenium tetroxide is a strong oxidant and therefore readily reacts with any exposed tungsten and/or tungsten oxide layers to form a consistent and catalytic active layer of ruthenium oxide or metallic ruthenium. An example of an exemplary process used to form ruthenium tetraoxide and deposit a ruthenium containing layer on the surface of the substrate is further described in the commonly assigned U.S. patent application Ser. No. 11/228,425, filed Sep. 15, 2005, which is incorporated by reference in its entirety. In one example, ruthenium tetroxide is formed by flowing an ozone containing gas, preferably >12 vol % ozone, across a metallic ruthenium source material (e.g., powdered ruthenium metal). The formed ruthenium tetraoxide is then delivered and separated from the other components in the ruthenium tetraoxide containing gas by use of a cold trap. Thereafter, the cold trap is purged of the unwanted gases and then warmed to a temperature to sublime the ruthenium tetroxide while a flow of inert gas is passed therethrough. The vaporized ruthenium tetroxide saturates the inert gas to form a ruthenium tetraoxide deposition gas. In an exemplary vapor deposition process, a deposition gas containing ruthenium tetroxide is delivered to a substrate having a tungsten oxide layer formed thereon. During the process, the substrate is maintained at a temperature between of about 100° C. and about 450° C., and more preferably a temperature between about 200° C. and about 400° C. A ruthenium containing layer can be selectively or non-selectively deposited on certain preferred materials by adjusting the temperature of the substrate during processing (e.g., <180° C. (selective); >200 (non-selective)). After exposing the tungsten oxide layer to the ruthenium tetroxide containing gas for about 30 seconds, a ruthenium oxide layer is formed on the tungsten oxide layer.
In
Next the fill material 320 is deposited on the ruthenium-containing layer 318 to fill gap 310 as illustrated in
Dielectric Gap Fill Process
In an alternative embodiment, the gap 310 is filled with a dielectric material as illustrated by cross-sectional views shown in FIGS. 3A, 3I-3K.
In one example, dielectric fill material 330 is spin-on-glass (SOG) deposited by a spin-coating process. Dielectric fill material 330 containing SOG is formed by a polymerization reaction of precursor compounds that are dissolved in an organic solution. The isolated dielectric compound is useful to fill gap 310. Preferably, dielectric fill material 330 is a silicate or a polysiloxane and may contain a metal such as titanium, zirconium hafnium and/or vanadium. Therefore, the composition of a SOG used as dielectric fill material 330 may include silicon, carbon, oxygen, titanium, zirconium, hafnium, vanadium or combinations thereof. Substrate 300 is generally exposed to a thermal annealing, or curing, process following the SOG deposition process. Additional compositions of SOG and processes to deposit SOG into vias or trenches is described in J. W. Lutze et al., “Spin-on-glass for 200 nm trench isolation structures,” J. Micromech. Microeng, vol. 1, pp. 46-51 (1991), which is herein incorporated by reference.
In another example, dielectric fill material 330 is a silicon-containing material or a metal-containing material deposited by an ALD process or a CVD process. Examples of dielectric fill material 330 deposited by vapor deposition processes include silicon oxide, silicon oxynitride, aluminum oxide, tantalum oxide, hafnium oxide, hafnium silicate, zirconium oxide, zirconium silicate, titanium oxide, titanium silicate, derivates thereof and combinations thereof. Additional compositions of dielectric fill material 330 and vapor deposition processes to deposit dielectric fill material 330 is described the commonly assigned U.S. patent application Ser. No. 10/406,833, entitled, “Method for Hafnium Silicon Oxynitride Deposition,” filed Apr. 4, 2003, and published as U.S. Publication No. 20030235961 and U.S. patent application Ser. No. 11/127,767, entitled, “Apparatuses and Methods for Atomic Layer Deposition of Hafnium-Containing High-K Materials,” filed May 12, 2005, which are both herein incorporated by reference.
A planarization process, such as a chemical mechanical polishing (CMP) process or etching process may be performed to remove an excess dielectric fill material 330 deposited on the surface of substrate 300 (i.e., field region 307) and expose the upper surface tungsten layer 306, as depicted in
Preferably, the dielectric fill material 330 is formed from a material that does not readily deform, form an alloy with the conductive layer 350, or change state so that the physical properties or electrical properties of the material in the dielectric fill material 330 remain unchanged after subsequent semiconductor processing steps have been performed on the substrate. It is generally desirable to fill the gap 310 so that no gaps or voids are formed in the plug 303 or plug 321, and thus integrity of conductive layer 350 is preserved during subsequent semiconductor processing steps. In one aspect, the material used to form the dielectric fill material 330 is selected so that it can withstands exposure to temperature of about 500° C. or higher, preferably about 700° C. or higher, and more preferably about 1,000° C. or higher.
The process steps illustrated in
Interconnect Formation Process
In another embodiment, a process is used to initiate on a tungsten containing contact plug to form an interconnect feature (see item # 321 in
The dielectric layer 420 and the dielectric surface 418 are composed of a dielectric material that may include silicon dioxide, silicon nitride, SOI, silicon oxynitride and/or carbon-doped silicon oxides, such as SiOxCy, for example, BLACK DIAMOND™ low-k dielectric, available from Applied Materials, Inc., located in Santa Clara, Calif. The dielectric material forming dielectric layer 420 and dielectric surface 418 may be deposited by a vapor deposition process such as CVD or plasma-enhanced-CVD (PE-CVD). In one example, a TEOS CVD process, utilizing the precursor tetraethyl orthosilicate (Si(OC2H5)4 or TEOS), is conducted to deposit a silicon oxide material at about 700° C. In another example, a TEOS PE-CVD process is conducted to deposit a silicon oxide material at about 500° C.
In one embodiment, not shown in
Thereafter, as illustrated in
Alternate Interconnect Formation Process
In another embodiment, a process is used to initiate on a tungsten containing contact plug to form an interconnect feature 505.
In one embodiment, not shown in
Pretreatment Process Example
In one embodiment of the pretreatment process, various processing steps 3000 (see
In the first step of the pretreatment process, or step 3002, the surface 512 is exposed to a clean solution to remove leftover etch residues from the formation of the interconnect feature 505 and/or any left over dielectric material (Item # 520
In the second step of the pretreatment process, or step 3003, the surface 512 is exposed to surface preparation step that is adapted to further normalize the surface 512 prior to performing the subsequent deposition steps. It is believed that exposure of the surface 512 to a tungstate source will tend to normalize the activity of all the exposed regions across the substrate surface so that they all behave similarly in the subsequent processing steps. In this step a preparation solution containing tungstic acid (H2WO4) and/or various tungstate salts, or other water soluble WO42− sources, hydrates thereof, derivatives thereof or combinations thereof are dispensed on the substrate surface to promote the bonding of the subsequent layers to the substrate surface. In one aspect, the preparation solution contains tungstic acid in a concentration between about 0.002 M and about 0.1 M, and has an adjusted pH of between about 12 and about 13 by the addition of a base (e.g., TMAH). Preferably, the tungstic acid concentration in the preparation solution is between about 0.06 and about 0.1 M and the pH is about 12.5. In one aspect, the preparation solution is dispensed on the surface of the substrate at a temperature at or near room temperature (e.g., ˜20° C.). The time the preparation solution is in contact with the surface of the substrate to achieve a desired result may depend on the prior processing steps the substrate has gone through and the concentration of the processing solution components. For example, an aqueous solution that contains about 10 g/l of tungstic acid and has adjusted pH of about 12.5 may only require between about a 30 second and about a 45 second exposure to the substrate surface.
In the third step of the pretreatment process, or step 3004, prior to the deposition of the bulk fill layer 550 the surface 512 is activated using an activation solution. During this step, an initiation layer (not shown) may be formed on the surface 512 by displacement plating of a catalytic metal such a palladium, platinum, ruthenium, osmium, rhodium or iridium. Typical procedures for cleaning and displacement plating of tungsten with palladium employ dilute aqueous acid solutions of palladium salts such as palladium chloride, palladium nitrate or palladium sulfate. An example of a suitable acidic activation solution is one prepared by addition of about 4 ml of a 10 wt % Pd(NO3)2 in 10% nitric acid to 1 liter of deionized water. In another example, an activation solution contains about 120 ppm palladium chloride and sufficient hydrochloric acid to provide a pH in a range from about 1.5 to about 3. Substrates to be activated are exposed to the activation solution for about 30 seconds at room or ambient temperature.
Next an optional rinse process (step 3005) is used to activate the initiation layer, clean the substrate surface and/or remove remaining contaminants from any of the early processes. In this step a rinse activation solution is dispensed on the substrate surface to activate the initiation layer formed in the third step. In one aspect, the rinse activation solution is a reducing solution (e.g., DMAB, glyoxylic acid) that is delivered to the substrate surface for wetting, cleaning and thermally equilibrating the substrate surface. In one aspect, one liter of a rinse activation solution containing about 1.2 g DMAB and about 3.3 g of 50% H3PO2 to DI water at ambient temperature, and enough 25% TMAH to adjust the pH to about 9.25, is dispensed on the substrate surface. In another aspect, a rinse activation solution may contain about 1.2 g/L DMAB, 7.2 g/L of citric acid, 0.1 g/L of hydroxypyridine (a stabilizer), and about 3.3 g/L of 50% H3PO2, DI water, and then adding 25% TMAH to adjust the pH to about 9.25. In one aspect, the rinse activation solution contains DMAB in a concentration from about 1 mM to about 200 mM, and preferably, about 20 mM. In one example, the rinse process may be for about 30 seconds.
Next an optional chelating process (step 3006) that uses a chelating solution is dispensed on the substrate surface to clean the substrate surface and/or remove remaining contaminants from any of the early processes. The chelating solution is used to remove and prevent particles from forming on the activated surface. In one aspect, a room temperature chelating solution containing about 0.1 M of citric acid is dispensed on and/or remains in contact with the substrate surface for about 30 seconds.
One will note that a rinse process will general follow each process steps described above, to reduce the interaction of the various chemicals. The rinse process includes rinsing the substrate surface with deionized water at or near room temperature. The substrate will be rinsed for a period from about 1 second to about 30 seconds, preferably from about 5 seconds to about 10 seconds.
Referring to
In another embodiment, as shown in
Examples of Electroless Process Solutions
The following are a examples of various electroless chemistries and processes that may be used to form the fill material 230, fill material 320, seed/adhesion layer 325, conductive layer 350, seed layer 440, bulk fill layer 450, seed layer 540, and/or bulk fill layer 550.
Electroless Nickel Deposition Chemistries and Processes
In one example, an electroless deposition solution useful to form nickel-containing material contains a nickel source, a reductant, at least one complexing agent, a pH adjusting agent, water and optional additives and surfactants. Nickel-containing material may be deposited by an electroless process utilizing either a pre-mixed electroless deposition solution or an in-line mixing process that combines solution components to generate the electroless solution.
The nickel source within the electroless deposition solution may have a concentration within a range from about 20 mM to about 200 mM, preferably from about 40 mM to about 80 mM, and more preferably from about 50 mM to about 70 mM, such as about 60 mM. Nickel sources provide nickel ions (e.g., Ni2+) dissolved within the electroless solution and later reduced out as the deposited nickel-containing material. Useful nickel sources include nickel sulfate, nickel chloride, nickel acetate, nickel phosphate, derivatives thereof, hydrates thereof or combinations thereof. In a preferred embodiment, nickel sulfate hexahydrate (NiSO4.6H2O) is used in the electroless solution to deposit nickel-containing materials.
The reductant within the electroless deposition solution may have a concentration within a range from about 1 mM to about 100 mM, preferably from about 2 mM to about 50 mM, and more preferably from about 5 mM to about 20 mM, such as about 14 mM. Reductants provide electrons to induce chemical reduction of the nickel ions that form and deposit the nickel-containing material. Reductants may include organic reductants (e.g., formaldehyde or glyoxylic acid), hydrazine, organic hydrazines (e.g., methyl hydrazine), hypophosphite sources (e.g., hypophosphorous acid (H3PO2), ammonium hypophosphite ((NH4)4-xHxPO2) and salts thereof), borane sources (e.g., dimethylamine borane complex ((CH3)2NH.BH3), DMAB), trimethylamine borane complex ((CH3)3N.BH3), TMAB), tert-butylamine borane complex (tBuNH2.BH3), tetrahydrofuran borane complex (THF.BH3), pyridine borane complex (C5H5N.BH3), ammonia borane complex (NH3.BH3), borane (BH3), diborane (B2H6), derivatives thereof, complexes thereof or combinations thereof. In a preferred embodiment, DMAB is used as a reductant in the electroless solution for depositing nickel-containing materials.
Chelators or complexing agents are in the electroless solution to complex nickel ions thereby stabilizing the solubility and reduction of nickel ions. The complexing agents may have a concentration within a range from about 50 mM to about 2 M, preferably from about 100 mM to about 1 M, and more preferably from about 200 mM to about 500 mM. Complexing agents generally may have functional groups, such as carboxylic acids, dicarboxylic acids, polycarboxylic acids, amino acids, amines, diamines, polyamines, alkylamines, alkanolamines and alkoxyamines. Complexing agents may include citric acid, citrates, glycolic acid, glycine, malonic acid, maleic acid, lactic acid, ethylenediaminetetraacetic acid (EDTA), ethylenediamine (EDA), triethylene tetramine (TETA), diaminoethane, monoethanolamine, diethanolamine (DEA), triethanolamine (TEA), hydroxylamine hydrochloride, ammonia, ammonium chloride, derivatives thereof, salts thereof or combinations thereof. Usually, the electroless solution contains more than one complexing agent. Preferably, the electroless solution contains at least citric acid or citrate salts, more preferably, the electroless solution also contains DEA, glycine and/or lactic acid. In one example, the electroless solution contains about 60 mM of citric acid, 60 mM of DEA, 15 mM of glycine and 120 mM of lactic acid.
A pH adjusting agent is added to adjust the electroless solution to a pH value within a range from about 8 to about 11, preferably from about 9 to about 10, and more preferably from about 8.0 to about 8.5, such as about 8.5. The pH adjusting agent may be an acidic compound to decrease the pH value of the electroless solution and include hydrochloric acid, sulfuric acid, phosphoric acid, derivatives thereof or combinations thereof. Alternatively, the pH adjusting agent may be a basic compound to increase the pH value of the electroless solution and include metal hydroxides, tetraalkylammonium hydroxides (e.g., tetramethylammonium hydroxide ((CH3)4NOH, TMAH) or tetraethylammonium hydroxide ((CH3CH2)4NOH, TEAH)), ammonium hydroxide, DEA, TEA, derivatives thereof or combinations thereof. The pH adjusting agent may be dissolved in water prior to adjusting the pH value of the electroless solution. In one example, a 25 wt % aqueous solution of TMAH is used as a pH adjusting agent. In another example, both TMAH and DEA are used to adjust the pH value of an electroless solution.
The optional additives may include levelers, accelerators and suppressors. Levelers within the electroless solution are used to achieve different deposition thickness as a function of leveler concentration and feature geometry while depositing nickel-containing materials. The leveler within the electroless deposition solution may have a concentration within a range from about 20 ppb to about 600 ppm, preferably from about 100 ppb to about 100 ppm. Examples of levelers that may be employed in an electroless solution include, but are not limited to alkylpolyimines and organic sulfonates, such as 1-(2-hydroxyethyl)-2-imidazolidinethione (HIT), 4-mercaptopyridine, 2-mercaptothiazoline, ethylene thiourea, thiourea or derivatives thereof. The electroless deposition solution may contain brighteners or accelerators and suppressors as alternative additives to provide further control of the deposition process. The role of accelerators is to achieve a smoothly deposited surface of the nickel-containing material. The accelerator within the electroless deposition solution has a concentration within a range from about 20 ppb to about 600 ppm, preferably from about 100 ppb to about 100 ppm. Accelerators that are useful in an electroless solution for depositing nickel-containing materials may include sulfur-based compounds such as bis(3-sulfopropyl)disulfide (SPS), 3-mercapto-1-propane sulfonic acid (MPSA), aminoethane sulfonic acids, thiourea, derivatives thereof, combinations thereof. Suppressors are used to suppress nickel deposition by initially adsorbing onto underlying catalytic surfaces and therefore blocking access to the catalyst of the reaction. Suppressors generally may include polyethylene glycol (PEG), polypropylene glycol (PPG), polyoxyethylene-polyoxypropylene copolymer (POCP), benzotriazole (BTA), dipyridyl, dimethyl dipyridyl, derivatives thereof or combinations thereof. The suppressor within the electroless deposition solution may have a concentration within a range from about 20 ppb to about 600 ppm, preferably from about 100 ppb to about 100 ppm.
The electroless solution may contain boric acid as an additional additive. Boric acid is added to provide additional buffering and to stabilize the composition of the solution. Boric acid is an oxidation by-product from the chemical reactions of borane reductants (e.g., DMAB). Therefore, an electroless solution containing boric acid is more normalized at the start of the deposition process since a less steep dissipation gradient exist as additional boric acid is formed from the borane reductant. Boric acid is preferably within the electroless deposition solution at concentration within a range from about 1 mM to about 50 mM, preferably from about 2 mM to about 20 M, and more preferably from about 3 mM to about 15 mM, such as about 5 mM.
Also, an optional surfactant may be added to the electroless solution. The surfactant is a wetting agent to reduce the surface tension between the electroless solution and the substrate surface. Surfactants are generally added to the electroless solution at a concentration of about 1,000 ppm or less, preferably about 800 ppm or less, such as from about 20 ppb to about 600 ppm. The surfactant may have ionic or non-ionic characteristics. A preferred surfactant includes dodecyl sulfates, such as sodium dodecyl sulfate (SDS). Other surfactants that may be used in the electroless deposition solution include glycol ether based surfactants (e.g., polyethylene glycol). For example, a glycol ether based surfactants may contain polyoxyethylene units, such as TRITON® 100, available from Dow Chemical Company. A nonylphenol ethoxylate surfactant is useful in the electroless deposition solution, such as TERGITOL®, available from Dow Chemical Company or IGEPAL-630, available from GAF Corporation. Other useful surfactants may contain phosphate units, for example, sodium poly(oxyethylene)phenyl ether phosphate, such as RHODAFAC® RE-610, available from Rhodia, Inc. The surfactants may be single compounds or a mixture of compounds of molecules containing varying length of hydrocarbon chains.
An electroless process to deposit nickel-containing materials may utilize an in-line mixing process to form the electroless solution. The process may contain the addition of two, three, four or more componential solutions to form the electroless solution. In one example, the electroless solution is formed by combining a buffered cleaning solution, a nickel-containing solution, a reducing solution and water, where each solution is a concentrate and water is added to reach a predetermined concentration of the final solution. In another example, the electroless solution is formed by combining a buffered cleaning solution, a nickel-containing solution and a reducing solution, where each of the solutions are pre-diluted and therefore do not require additional water. In another example, the electroless solution is formed by combining a buffered nickel-containing solution, a reducing solution and water, where a buffered cleaning solution and a nickel-containing solution are combined to form the buffered nickel-containing solution. Further details of in-line mixing processes and componential solutions are further described in the commonly assigned, U.S. patent application Ser. No. 10/967,919, entitled, “Selective Self-initiating Electroless Capping of Copper with Cobalt-containing Alloys,” filed on Oct. 18, 2004, and published as US 2005-0136193, which is incorporated by reference to the extent not inconsistent with the claimed aspects and description herein.
A buffered cleaning solution usually contains water, at least one complexing agent, additives and a pH adjusting agent. The complexing agent within the buffered cleaning solution is at a concentration from about 0.2 M to about 3 M, preferably from about 0.5 M to about 2 M. The additive within the buffered cleaning solution is at a concentration from about 10 mM to about 1 M, preferably from about 50 mM to about 500 mM. The pH adjusting agent is at a concentration to provide the buffered cleaning solution with a pH value in a range from about 7.5 to about 11, preferably from about 8 to about 10, and more preferably from about 9.2 to about 9.6, such as about 9.4. In one example, a buffered cleaning solution contains water, about 1.15 M of DEA, about 375 mM of citric acid, about 300 mM of glycine, about 100 mM of boric acid and a concentration of TMAH to adjust the pH value to about 9.4. In another example, a buffered cleaning solution contains water, about 330 mM of DEA, about 300 mM of citric acid, about 150 mM of glycine, about 50 mM of boric acid and a concentration of TMAH to adjust the pH value to about 9.4.
A nickel-containing solution usually contains water, a nickel source, at least one complexing agent and a pH adjusting agent. The nickel source within the nickel-containing solution is at a concentration from about 50 mM to about 1 M, preferably from about 100 mM to about 500 mM, such as about 300 mM. The complexing agent within the nickel-containing solution is at a concentration from about 0.2 M to about 2 M, preferably from about 0.5 M to about 1 M. The pH adjusting agent is at a concentration to provide the nickel-containing solution with a pH value in a range from about 8 to about 11, preferably from about 9 to about 10, and more preferably from about 8.0 to about 8.5, such as about 8.5. In one example, a nickel-containing solution contains water, about 100 mM of citric acid, about 300 mM of nickel sulfate, about 600 mM of 85% lactic acid and a concentration of TMAH to adjust the pH value to about 9.4.
A reducing solution usually contains water, at least one reductant, at least one complexing agent and a pH adjusting agent. The reductant within the reducing solution is at a concentration from about 10 mM to about 500 mM, preferably from about 50 mM to about 100 mM, such as about 70 mM. The complexing agent within the reducing solution is at a concentration from about 1 mM to about 50 mM, preferably from about 5 mM to about 15 mM, such as about 10 mM. The pH adjusting agent is at a concentration to provide the reducing solution with a pH value in a range from about 8 to about 11, preferably from about 9 to about 10, and more preferably from about 8.0 to about 8.5, such as about 8.5. In one example, a reducing solution contains water, about 10 mM of citric acid, about 70 mM of DMAB and a concentration of TMAH to adjust the pH value to about 9.4.
The electroless solution is preferably formed by in-line mixing process that combines various volumetric ratios of the buffered cleaning solution, the nickel-containing solution, the reducing solution and water. In one example, 1 volumetric equivalent of a buffered cleaning solution, 4 volumetric equivalents of a nickel-containing solution, 4 volumetric equivalents of a reducing solution and 11 volumetric equivalents of deionized water are in-line mixed to form an electroless solution. That is, the volumetric ratio of the buffered cleaning solution, the nickel-containing solution, the reducing solution and the deionized water is 1:4:4:11 (5%, 20%, 20%, 55% of electroless solution). In other examples of an electroless solution, a volumetric ratio of the buffered cleaning solution, the nickel-containing solution, the reducing solution and the water is 1:2:2:5 (10%, 20%, 20%, 50% of electroless solution) and 1:1:1:3 (16.7%, 16.7%, 16.7%, 50% of electroless solution).
In one embodiment, an electroless solution contains: nickel sulfate with a concentration in a range from about 20 mM to about 200 mM, preferably from about 40 mM to about 80 mM, and more preferably from about 50 mM to about 70 mM, such as about 60 mM; DMAB with a concentration in a range from about 1 mM to about 100 mM, preferably from about 2 mM to about 50 mM, and more preferably from about 5 mM to about 20 mM, such as about 14 mM; citric acid with a concentration in a range from about 5 mM to about 500 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 40 mM to about 80 mM, such as about 60 mM; DEA with a concentration in a range from about 5 mM to about 500 mM, preferably from about 10 mM to about 200 mM, such as about 60 mM; glycine with a concentration in a range from about 1 mM to about 150 mM, preferably from about 2 mM to about 80 mM, and more preferably from about 5 mM to about 50 mM, such as about 15 mM; boric acid with a concentration in a range from about 1 mM to about 100 mM, preferably from about 2 mM to about 50 mM, and more preferably from about 3 mM to about 20 mM, such as about 5 mM; lactic acid with a concentration in a range from about 10 mM to about 500 mM, preferably from about 50 mM to about 200 mM, and more preferably from about 100 mM to about 140 mM, such as about 120 mM; TMAH with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 9 to about 10, and more preferably from about 98.0 to about 8.5, such as about 8.5.
In one embodiment, citrate is a preferred complexing agent and is present in each componential solution, such as the buffered cleaning solution, the nickel-containing solution and the reducing solution. Citrate may be added as citric acid and/or as a citrate salt. Citrate plays an important role of buffering each of the individual componential solutions while being combined to form the plating solution. Citrates generally have poor solubility in water at high concentrations, while the componential solutions may have relatively concentrated solutions. If a substantial citrate concentration of the final electroless solution is desired, a single componential solution may not be capable of completely containing all the dissolved citrate. Therefore, the citrate may be dissolved in each componential solution to assure no formation of citrate precipitate, and subsequently combined with water forming the electroless solution at a final concentration.
The electroless deposition process may be conducted at a temperature in a range from about 35° C. to about 120° C., preferably from about 60° C. to about 100° C. In one example, the temperature is from about 80° C. to about 85° C. In another example, the temperature is from about 65° C. to about 70° C. The water may be degassed, preheated and/or deionized water. Degassing the water reduces the oxygen concentration of the subsequently formed electroless solution. An electroless solution with a low oxygen concentration (e.g., less than about 100 ppm) may be used during the deposition process. Preheated water allows forming the electroless solution at a predetermined temperature just below the temperature used to initiate the deposition process, thereby shortening the process time.
The substrate may be exposed to a chemical mechanical polishing (CMP) process prior to the pretreatment and deposition processes described herein. Usually, the CMP process is conducted in a first process chamber, the nickel-containing layer or cobalt-tungsten alloy layer is deposited in a second process chamber and the first and second process chambers are on the same CMP tool. In one example, the second process chamber is in fluid communication to an in-line mixing system that combines stock solutions used in the pretreatment process and/or the electroless deposition processes.
A “substrate surface” as used herein refers to any substrate or material surface formed on a substrate upon which film processing is performed. For example, a substrate surface on which processing may be performed include materials such as monocrystalline, polycrystalline or amorphous silicon, strained silicon, silicon on insulator (SOI), doped silicon, silicon germanium, germanium, gallium arsenide, glass, sapphire, silicon oxide, silicon nitride, silicon oxynitride and/or carbon doped silicon oxides, such as SiOxCy, for example, BLACK DIAMOND™ low-k dielectric, available from Applied Materials, Inc., located in Santa Clara, Calif. Substrates may have various dimensions, such as 200 mm or 300 mm diameter wafers, as well as, rectangular or square panes. Embodiments of the processes described herein deposit nickel-containing materials on many types of substrates and surfaces. Substrates on which embodiments of the invention may be useful include, but are not limited to semiconductor wafers, such as crystalline silicon (e.g., Si<100> or Si<111>), silicon oxide, strained silicon, silicon germanium, doped or undoped polysilicon, doped or undoped silicon wafers, and patterned or non-patterned wafers. Substrates made of glass or plastic, which, for example, are commonly used to fabricate flat panel displays and other similar devices, are also included.
A chamber useful to conduct an electroless deposition process for depositing a cobalt-tungsten material, a cobalt-nickel material or a nickel-containing material is the electroless deposition process cell, further described in the commonly assigned U.S. patent application Ser. No. 10/965,220, entitled “Apparatus for Electroless Deposition,” filed on Oct. 14, 2004, and published as US 2005-0081785, U.S. patent application Ser. No. 10/996,342, entitled, “Apparatus for Electroless Deposition of Metals on Semiconductor Wafers,” filed on Nov. 22, 2004, U.S. patent application Ser. No. 11/043,442, entitled, “Apparatus for Electroless Deposition of Metals onto Semiconductor Substrates,” filed on Jan. 26, 2005, and U.S. patent application Ser. No. 11/040,962, entitled “Method and Apparatus for Selectively Changing Thin Film Composition During Electroless Deposition in a Single Chamber,” filed on Jan. 22, 2005, which are each incorporated by reference to the extent not inconsistent with the claimed aspects and description herein.
Examples of Cobalt and Nickel Electroless Deposition Chemistries
Cobalt
In one embodiment, an electroless solution for depositing metallic cobalt contains: cobalt ions (Co2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; hydrazine hydrate with a concentration in a range from about 100 mM to about 2 M, preferably from about 200 mM to about 1 M, and more preferably from about 300 mM to about 700 mM, such as about 500 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 200 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 30 mM to about 70 mM, such as about 50 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 10 to about 14, preferably from about 11.5 to about 13, and more preferably from about 12.2 to about 12.8, such as about 12.5. In one example, a pH value is about 11.5 or higher, preferably, about 12.0 or higher, and more preferably, about 12.5 or higher. The electroless deposition process to deposit metallic cobalt may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 90° C., and more preferably from about 70° C. to about 80° C., such as about 75° C.
Cobalt Boride
In one embodiment, an electroless solution for depositing cobalt boride contains: cobalt ions (Co2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; DMAB with a concentration in a range from about 1 mM to about 200 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 30 mM to about 50 mM, such as about 40 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 500 mM, preferably from about 30 mM to about 300 mM, and more preferably from about 50 mM to about 150 mM, such as about 100 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 8 to about 10, and more preferably from about 8.5 to about 9.5, such as about 8.9. The electroless deposition process to deposit cobalt boride may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 80° C., and more preferably from about 65° C. to about 75° C., such as about 70° C.
Cobalt Tungsten Boride
In one embodiment, an electroless solution for depositing cobalt tungsten boride contains: cobalt ions (Co2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; tungstic acid or tungstate salt with a tungstate concentration in a range from about 0.1 mM to about 10 mM, preferably from about 0.5 mM to about 5 mM, and more preferably from about 1 mM to about 3 mM, such as about 2 mM; DMAB with a concentration in a range from about 1 mM to about 200 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 30 mM to about 50 mM, such as about 40 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 500 mM, preferably from about 30 mM to about 300 mM, and more preferably from about 50 mM to about 150 mM, such as about 100 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 8 to about 10, and more preferably from about 8.5 to about 9.5, such as about 8.9. The electroless deposition process to deposit cobalt tungsten boride may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 80° C., and more preferably from about 65° C. to about 75° C., such as about 70° C.
Nickel Boride
In one embodiment, an electroless solution for depositing nickel boride contains: nickel ions (Ni2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 80 mM, such as about 60 mM; DMAB with a concentration in a range from about 1 mM to about 200 mM, preferably from about 10 mM to about 50 mM, such as about 28 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 300 mM, preferably from about 10 mM to about 60 mM, such as about 58 mM; boric acid with a concentration in a range from about 1 mM to about 100 mM, preferably from about 2 mM to about 50 mM, and more preferably from about 3 mM to about 20 mM, such as about 5 mM; lactic acid or lactate salt with a lactate concentration in a range from about 5 mM to about 300 mM, preferably from about 10 mM to about 150 mM, such as about 120 mM; glycine with a concentration in a range from about 1 mM to about 150 mM, preferably from about 2 mM to about 80 mM, and more preferably from about 5 mM to about 50 mM, such as about 15 mM; diethanolamine (DEA) with a concentration in a range from about 5 mM to about 300 mM, preferably from about 10 mM to about 150 mM, such as about 58 mM and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 8 to about 10, and more preferably from about 8.0 to about 8.5, such as about 8.5. The electroless deposition process to deposit nickel boride may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 80° C., and more preferably from about 65° C. to about 75° C., such as about 70° C.
Nickel Tungsten Boride
In one embodiment, an electroless solution for depositing nickel tungsten boride contains: nickel ions (Ni2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; tungstic acid or tungstate salt with a tungstate concentration in a range from about 0.1 mM to about 10 mM, preferably from about 0.5 mM to about 5 mM, and more preferably from about 1 mM to about 3 mM, such as about 2 mM; DMAB with a concentration in a range from about 1 mM to about 200 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 30 mM to about 50 mM, such as about 40 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 300 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 40 mM to about 60 mM, such as about 50 mM; lactic acid or lactate salt with a lactate concentration in a range from about 5 mM to about 300 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 40 mM to about 60 mM, such as about 50 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 8 to about 10, and more preferably from about 8.5 to about 9.5, such as about 8.9. The electroless deposition process to deposit nickel tungsten boride may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 80° C., and more preferably from about 65° C. to about 75° C., such as about 70° C.
Cobalt Nickel Boride
In one embodiment, an electroless solution for depositing cobalt nickel boride contains: cobalt ions (Co2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; nickel ions (Ni2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; DMAB with a concentration in a range from about 1 mM to about 200 mM, preferably from about 10 mM to about 100 mM, and more preferably from about 30 mM to about 50 mM, such as about 40 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 500 mM, preferably from about 30 mM to about 300 mM, and more preferably from about 50 mM to about 150 mM, such as about 100 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 8 to about 11, preferably from about 8 to about 10, and more preferably from about 8.5 to about 9.5, such as about 8.9. The electroless deposition process to deposit cobalt nickel boride may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 80° C., and more preferably from about 65° C. to about 75° C., such as about 70° C.
Cobalt Nickel
In one embodiment, an electroless solution for depositing cobalt nickel contains: cobalt ions (Co2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; nickel ions (Ni2+) with a concentration in a range from about 1 mM to about 100 mM, preferably from about 5 mM to about 50 mM, and more preferably from about 10 mM to about 20 mM, such as about 15 mM; hydrazine hydrate with a concentration in a range from about 100 mM to about 2 M, preferably from about 200 mM to about 1 M, and more preferably from about 300 mM to about 700 mM, such as about 500 mM; citric acid or citrate salt with a citrate concentration in a range from about 5 mM to about 500 mM, preferably from about 30 mM to about 300 mM, and more preferably from about 50 mM to about 150 mM, such as about 100 mM; and an optional pH adjusting agent (e.g., TMAH) with a concentration to adjust the electroless solution to a have pH value in a range from about 10 to about 14, preferably from about 11.5 to about 13, and more preferably from about 12.2 to about 12.8, such as about 12.5. The electroless deposition process to deposit cobalt nickel may be conducted at a temperature within a range from about 35° C. to about 100° C., preferably from about 60° C. to about 90° C., and more preferably from about 70° C. to about 80° C., such as about 75° C.
While foregoing is directed to the preferred embodiment of the invention, other and further embodiments of the invention may be devised without departing from the basic scope thereof, and the scope thereof is determined by the claims that follow.
This application claims benefit of U.S. Provisional Patent Application Ser. No. 60/663,493, filed Mar. 18, 2005 [APPM 9916L], U.S. Provisional Patent Application Ser. No. 60/683,599, filed May 23, 2005 [APPM 9916L02], U.S. Provisional Patent Application Ser. No. 60/703,538, filed Jul. 29, 2005 [APPM 9916L03], U.S. Provisional Patent Application Ser. No. 60/703,633, filed Jul. 29, 2005 [APPM 9916L04], U.S. Provisional Patent Application Ser. No. 60/709,564, filed Aug. 19, 2005 [APPM 9916L05], and U.S. Provisional Patent Application Ser. No. 60/754,230, filed Dec. 27, 2005 [APPM 9916L06], which are all herein incorporated by reference.
Number | Date | Country | |
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60663493 | Mar 2005 | US | |
60683599 | May 2005 | US | |
60703538 | Jul 2005 | US | |
60703633 | Jul 2005 | US | |
60709564 | Aug 2005 | US | |
60754230 | Dec 2005 | US |