Patent Grant
7220296
In the manufacture of integrated circuits, copper interconnects are generally formed on a semiconductor substrate using a copper damascene process (e.g., a dual damascene process which is well known in the art). In this process, a trench is etched into a dielectric layer and the trench is filled with a conventional barrier and seed layer. An electroplating process may then be used to fill the trench with copper metal to form the interconnect.
As device dimensions scale down, the aspect ratio of features such as trenches and vias becomes more aggressive as the feature becomes more narrow. Conventional processes for depositing copper into these features include PVD, chemical vapor deposition (CVD), atomic layer deposition (ALD), and electroplating. Unfortunately, the aggressive aspect ratios give rise to issues such as trench overhang, thereby resulting in pinched off the trench openings that cause voids to appear within the copper interconnect. Such voids may greatly increase the resistivity of the interconnect line.
Electroless deposition processes have been used to address issues with high aspect ratio features. Other issues, however, tend to arise such as unstable copper baths with narrow temperature windows and narrow pH windows and copper metal corrosion or pitting due to the long nucleation times needed to fill the high aspect ratio features. Furthermore, important secondary issues need to be considered such as high monetary costs and potential health hazards associated with the plating bath components. For instance, glyoxylic add, which is an important component of conventional plating baths, is a very expensive chemical. Alternates to glyoxylic acid tend to be expensive, carcinogenic, or both. Accordingly, an improved electroless copper deposition chemistry is needed to address the drawbacks present when electrolessly plating copper into high aspect ratio features, for instance, features having a width of between 5 nm and 20 nm and an aspect ratio greater than five.
Described herein are electroless plating baths for performing an electroless copper deposition into high aspect features. In the following description, various aspects of the illustrative implementations will be described using terms commonly employed by those skilled in the art to convey the substance of their work to others skilled in the art. However, it will be apparent to those skilled in the art that the present invention may be practiced with only some of the described aspects. For purposes of explanation, specific numbers, materials and configurations are set forth in order to provide a thorough understanding of the illustrative implementations. However, it will be apparent to one skilled in the art that the present invention may be practiced without the specific details. In other instances, well-known features are omitted or simplified in order not to obscure the illustrative implementations.
Various operations will be described as multiple discrete operations, in turn, in a manner that is most helpful in understanding the present invention, however, the order of description should not be construed to imply that these operations are necessarily order dependent. In particular, these operations need not be performed in the order of presentation.
Electroless plating is a metal deposition process in which the metal begins in solution and a controlled chemical reduction reaction is used to deposit the metal onto a substrate. The electroless process is autocatalytic as the metal being deposited catalyzes the chemical reduction reaction without the need for an external electric current. Electroless plating is a selective deposition and occurs at activated locations on the substrate surface, i.e., locations that have a nucleation potential for an electroless plating bath.
As is known in the art, preparing or treating a surface may be necessary to produce an activated surface. In some implementations, a metal seed layer may be deposited to serve as the activated surface upon which the electroless deposition may occur. This metal seed layer may be deposited using methods such as PVD, CVD, or conventional electroless processes. The activated surface acts as a region that controls the placement of the electrolessly deposited metal since the metal from the electroless plating bath deposits only on the activated surface. The inherent selectivity of the electroless plating process not only results in a substantially void free metal layer, but also results in a higher quality metal layer with improved uniformity and continuity.
The electroless plating bath generally includes water, a water soluble compound containing the metal to be deposited (e.g., a metal salt), a complexing agent (e.g., an organic acid or amine) that prevents chemical reduction of the metal ions in solution while permitting selective chemical reduction on a surface of the target, and a chemical reducing agent for the metal ions (e.g., hypophosphite, dimethylaminoborane (DMAB), formaldehyde, hydrazine, or borohydride). Additionally, the plating bath may include a buffer (e.g., boric acid, an organic add, or an amine) for controlling pH and various optional additives, such as bath stabilizers (e.g., pyridine, thiourea, or molybdates), surfactants (e.g., a glycol), and wetting agents. It is to be understood that the composition of a plating bath will vary depending on the desired plating outcome.
Implementations of the invention provide an electroless copper chemistry for depositing copper metal into narrow features, such as trenches and vias found on a semiconductor substrate, that have high aspect ratios. In some implementations, the aspect ratio for such features may be five or greater. Implementations of the invention also provide a stable plating bath with relatively lower costs and relatively lower health hazards. To deposit copper metal into features having high aspect ratios, implementations of the invention use a novel electroless plating bath. For instance, the electroless deposition process may use an electroless plating bath with a composition that includes, but is not limited to, water, a water-soluble copper-containing compound, a buffering agent, at least two reducing agents, a grain refining additive, a bath stabilizing agent, and a rate controlling additive.
A water-soluble copper-containing compound may be added to the water (204). The water-soluble copper-containing compound may be may be a copper salt. For example, in some implementations the copper salt may be cupric sulfate (e.g., CuSO4), and in other implementations the copper salt may be copper chloride (e.g., CuCl2). The copper salt provides the copper that will be deposited onto the substrate by the electroless plating process. As will be appreciated by those of skill in the art, alternate copper salts not mentioned here may be used as well. Once added to the water, the copper salt, such as copper sulfate or copper chloride, may have a concentration that is between 0.5 gram/liter (g/L) and 50 g/L in the electroless plating bath of the invention.
A buffering agent may be added to the water (206). In implementations of the invention, the buffering agent may consist of one or more compounds that are well known in the art as buffers for electroless plating baths. For instance, in implementations of the invention, buffering agents that may be used in the bath include, but are not limited to, ethylene diamine tetraacetic acid (EDTA), hydroxyethylene diamine triacetic acid (HEDTA), Rochelle salt (also known as potassium sodium tartarate), an organic acid (e.g., citric acid, tartaric acid, etc.), ammonium citrate, lactate, triethanolamine (TEA), and ethylene diamine. As will be appreciated by those of skill in the art, alternate buffering agents not mentioned here may be used as well. Once added to the water, the buffering agent may have a concentration that is between 25 g/L and 100 g/L in the electroless plating bath of the invention. In general, the concentration of buffering agent will be directly proportional to the concentration of the copper-containing compound.
In accordance with an implementation of the invention, a dual reducing agent formulation may be used in the electroless plating bath. One reducing agent that is added to the water may consist of a bulk reducing agent that is stable and relatively inexpensive (208). The bulk reducing agent makes up the majority of the reducing agent that is added to the electroless plating bath and may or may not be able adequately initiate the reducing chemistry. The other reducing agent that is added to the water may consist of a catalyst reducing agent that is capable of adequately initiating the reducing chemistry (210). A relatively small amount of the catalyst reducing agent is used as the catalyst reducing agent tends to be relatively expensive. Once the reducing chemistry is initiated, the process becomes self-activated. The catalyst reducing agent and the bulk reducing agent may be added simultaneously or separately.
In some implementations, a combination of glycolic acid and glyoxylic acid may be used. Glycolic acid is a stable, less hazardous, and relatively inexpensive reducing agent. The use of glycolic acid in the plating bath may substantially reduce the overall cost of the bath. Glycolic acid may be used as the bulk reducing agent, however, glycolic acid cannot be used as the sole reducing agent because it cannot adequately initiate the reducing chemistry. Therefore, a minimal amount of a catalyst reducing agent, such as glyoxylic acid, is used to initiate the reducing chemistry. Glyoxylic acid is able to adequately initiate the reducing chemistry but glyoxylic acid tends to be an expensive reducing agent. In implementations of the invention, however, this cost is substantially reduced because only a relatively small amount of glyoxylic acid is needed. In some implementations, the glyoxylic acid may be added to the water in a monohydrate form. In alternate implementations, the glyoxylic acid may be added to the water in the form of a solution, for example, as a 50% solution of glyoxylic acid.
In some implementations, the glycolic acid may constitute 95% to 99% of the reducing agent in the plating bath of the invention, while the glyoxylic acid may constitute the remaining 1% to 5% of the reducing agent. In some implementations, the total reducing agent may have a concentration that is between 2.5 g/L and 30 g/L in the electroless plating bath of the invention. Therefore, the glycolic acid content of the reducing agent may range from approximately 2.37 g/L to approximately 29.7 g/L. Similarly, the glyoxylic acid content of the reducing agent may range from approximately 0.02 g/L to approximately 1.5 g/L. As will be recognized by one of ordinary skill in the art, the amount of glyoxylic acid used in the electroless plating bath of the invention is substantially lower than the amount used in conventional plating baths.
In another implementation of the invention, the reducing agent may consist of a combination of a hypophosphite and glyoxylic acid. Similar to the glycolic acid, the hypophosphite is a relatively inexpensive material that can function as the reducing agent but cannot adequately initiate the reducing chemistry. Therefore, a catalyst reducing agent, such as glyoxylic acid, is needed. Examples of hypophosphites that may be used include, but are not limited to, sodium hypophosphite and ammonium hypophosphite. Much like glycolic add, hypophosphites are relatively stable, safe, and relatively inexpensive. Also like glycolic acid, hypophosphites cannot be used as the sole reducing agent, therefore, a minimal amount of glyoxylic add is used in combination with the hypophosphites. In some implementations, the hypophosphite may constitute 95% to 99% of the reducing agent in the plating bath of the invention, while the glyoxylic add may constitute the remaining 1% to 5% of the reducing agent. The total reducing agent may have a concentration that is between 5 g/L and 30 g/L in the electroless plating bath of the invention. Therefore, the hypophosphite content of the reducing agent may range from approximately 2.37 g/L to approximately 29.7 g/L. Similarly, the glyoxylic acid content of the reducing agent may range from approximately 0.02 g/L to approximately 1.5 g/L.
In alternate implementations of the invention, the glyoxylic acid may be replaced with alternate reducing agents that may be used in combination with glycolic add or hypophosphite. Examples of glyoxylic acid replacements in the electroless plating bath of the invention include, but are not limited to, DMAB, hydrazine, borohydride, as well as any other well known metal reducing agent. As will be appreciated by those of skill in the art, alternate reducing agents not mentioned here may be used with the glycolic add or the hypophosphite.
Conventional electroless plating baths generally rely on an expensive reducing agent such as glyoxylic add to function as the sole reducing agent for the entire bath. This drives up the cost of the bath. Unlike conventional baths, the electroless plating bath of the invention uses a dual reducing agent system in which a relatively inexpensive reducing agent makes up the bulk of the reducing agent in the bath, while only a small amount of a relatively expensive reducing agent is used to start or initiate the reducing chemistry.
A grain refining additive may be added to the water (212). In implementations of the invention, the grain refining additive may be a high molecular weight compound that is capable of reducing the grain size of the plated copper metal. By reducing the grain size of the copper, the copper metal may more readily enter high aspect features and reach the bottom of the features while minimizing issues such as obstructing the trench gap or forming a trench overhang. In implementations of the invention, materials that may be used as the grain refining additive include, but are not limited to, polyethylene glycol (PEG), ethylene diamine, propionitrile (also known as ethyl cyanide), and ethylene glycol (EG). Some of these materials may be available in polymeric form, such as PEG which may be available as PEG 2000, PEG 4000, PEG 6000, etc. In accordance with implementations of the invention, the grain refining additive may have a molecular weight that ranges from 1,000 to 10,000. As will be appreciated by those of skill in the art, alternative high molecular weight compounds capable of reducing the grain size of the plated copper metal may be used. Once added to the water, the grain refining additive may have a concentration that is between 0.25 g/L and 5.0 g/L.
A bath stabilizing agent may be added to the water (214). In implementations of the invention, the bath stabilizing agent may consist of one or more compounds that are capable of stabilizing the bath against the formation of undesired cuprous oxide particles for electroless plating processes having relatively long nucleation times. The long nucleation times help to completely fill features with high aspect ratios. In some implementations, the bath stabilizing agent may further function as a leveling agent to produce mirror-like plated surfaces. In implementations of the invention, bath stabilizing agents that may be used include, but are not limited to, thiourea, dypiridil, mercaptobenzothiazole (MBT), benzotriazole, Janus Green B (JGB), cyanide, vanadium pentoxide (V2O5), as well as certain high molecular weight polymers. Once added to the water, the bath stabilizing agent may have a concentration that is between 0.02 g/L and 0.1 g/L. In alternate implementations, aeration may be used as a stabilizer.
A rate controlling additive may be added to the water (216). In implementations of the invention, the rate controlling additive may consist of one or more compounds that are capable of suppressing the deposition rate of copper metal in certain portions of the substrate while increasing the deposition rate of the copper metal in other portions of the substrate. This may be necessary to fill high aspect ratio features. For example, a bottom-up fill process (also known as superfill) may be used to fill high-aspect features by suppressing the copper deposition rate at the surface of the substrate (often referred to as the “field”), while simultaneously increasing the copper deposition rate within the narrow trenches and vias. Once added to the water, the rate controlling additive may have a concentration that is between 0.01 g/L and 0.5 g/L.
In some implementations, certain rate controlling additives may function to both increase the copper deposition rate within the features while suppressing the copper deposition rate on the field. For instance, certain polymeric additives, such as PEG, may become anchored to the field by techniques that are well known in the art, such as the use of a metal catalyst as an anchoring agent. The anchored polymeric additive substantially prevents copper from depositing on at least portions of the field, thereby suppressing the copper deposition rate at the surface of the substrate. Suppressing metal deposition on the field forces the metal to travel down into the narrow trenches where the metal deposits and fills the gap. The polymeric additive generally does not inhibit metal deposition within the features, such as the narrow trenches and vias, because the size of the high molecular weight polymer substantially prevents it from entering such features. The polymeric additive therefore increases copper deposition within the features by suppressing copper deposition on the top surface.
In some implementations, certain rate controlling additives may be used to suppress the copper deposition rate in areas while other rate controlling additives may be used to increase the copper deposition rate in other areas. For instance, rate controlling additives that may be used to suppress the copper deposition rate on the field include, but are not limited to, polyethers such as polyethylene glycol (PEG), polypropylene glycol (PPG), nitrogen bearing heterocyclic or non-heterocyclic aromatic compounds, large molecular weight polyoxy-alkyl type compounds, and other high molecular weight polymers. Furthermore, rate controlling additives that may be used primarily to increase the copper deposition rate within high-aspect features include, but are not limited to, sulfur-based organic molecules such as bis(sodiumsulfopropyl) disulfide (SPS), other disulfides, and surfactants.
In some implementations, a high molecular weight polymer may be used as a grain refining additive as well as a rate controlling additive. For instance, in some implementations, PEG may be used as both a grain refining additive and a rate controlling additive.
In addition to promoting superfill, the use of rate controlling additives allows the nucleation time to be controlled without having to rely on adjustments to the pH level and/or temperature of the electroless plating bath, as is done in conventional processes. Furthermore, the use of rate controlling additives allows the nucleation time to be varied across the different areas of the substrate (i.e., suppressing the deposition rate on the field while increasing the deposition rate within the features), which cannot be readily accomplished by adjusting the pH level and temperature of the bath. Finally, the use of rate controlling additives enables the electroless plating bath of the invention to be used over a wider pH range and a wider temperature range than conventional processes. For instance, in some implementations, the electroless plating bath described herein may be used within a pH range of pH 10 to pH 12 and a temperature range of 60° C. to 80° C. As will be appreciated by those of skill in the art, alternate rate controlling additives not mentioned here may be used as well.
After the above listed constituents are added, the plating bath may be agitated (218). The agitation time may range from 30 minutes to 90 minutes. The plating bath may also be filtered (220). The filter size used may vary based on a number of factors, but will generally range from 0.01 microns to 1.0 micron.
Different combinations of the above listed constituents that include at least one water-soluble copper-containing compound, at least one buffering agent, at least two reducing agents, at least one grain refining additive, at least one bath stabilizing agent, and at least one rate controlling additive may be used to form electroless plating baths in accordance with implementations of the invention. For instance, in one implementation, the electroless plating bath may include water, 0.5 to 50 g/L of CuSO4, 25 to 100 g/L of EDTA, 0.13 to 1.5 g/L of glyoxylic acid, 2.38 to 28.5 g/L of glycolic acid, 0.25 to 5 g/L of ethylene diamine, 0.02 to 0.1 g/L of MBT, and 0.01 to 0.5 g/L of PEG. And in another implementation, the electroless plating bath may include water, 0.5 to 50 g/L of CuCl2, 25 to 100 g/L of Rochelle salt, 0.13 to 1.5 g/L of glyoxalic acid, 2.38 to 28.5 g/L of hypophosphite, 0.25 to 5 g/L of PEG, 0.02 to 0.1 g/L of thiourea, and 0.01 to 0.5 g/L of SPS. Of course, many further combinations of the above provided constituents is possible.
A substrate containing narrow features to be filled with copper metal may be cleaned prior to being immersed in the electroless plating bath of the invention. In one implementation, such a cleaning process may include applying a mild acidic etchant to the substrate at a temperature between 20° C. and 60° C. and a pH level between pH 3 and pH 5. This cleaning process may remove native oxides or any contaminants from the substrate surface.
Electroless plating baths formed in accordance with implementations of the invention may be used in electroless plating processes to fill high aspect ratio features with copper metal. In some implementations, the surface of the substrate containing the features may include an activated surface to provide a nucleation potential for the electroless plating bath. In some implementations, the activated surface may be a thin conductive layer that may be non-conformal and may be non-continuous. The conductive layer may be deposited using conventional vapor deposition processes such as chemical vapor deposition, atomic layer deposition, or physical vapor deposition. Alternately, the activated surface may be deposited using an electroless process. In other implementations, the electroless plating bath of the invention may be a self-catalytic bath, rendering a conductive layer unnecessary. The surface of the substrate may be only a barrier material without any seed, such as tantalum nitride, tantalum, tungsten, tantalum alloy, as well as other known barrier materials. These substrates may be activated by conventional conductive metal deposition directly on the barrier layer.
In accordance with implementations of the invention, the electroless plating baths described herein may be used under an inert atmosphere when the electroless plating process is carried out. The inert atmosphere may consist of nitrogen, helium, argon, or forming gas. In some implementations, an electroless deposition process using the electroless plating bath of the invention may be carried out under an inert atmosphere with minimal or no delay between process steps. In various implementations, the electroless plating bath of the invention may be applied to the substrate using well known spray techniques, immersion processes, or semi-immersion processes, using tools that may or may not implement point-of-use solution mixing. In implementations, the substrate may be heated prior to the electroless deposition process by using hot chemistry or maintaining a sufficient electroless plating bath temperature.
As is well known in the art, a chemical mechanical polishing process may follow the electroless plating process to remove any excess metal and to planarize the substrate and metal surface, thereby completing formation of a copper interconnect.
Accordingly, electroless plating baths have been disclosed that provide improved copper metal deposition within features, such as trenches and vias, having aspect ratios of 6 or greater. Implementations of the invention described herein provide electroless plating baths that enable electroless plating processes having longer nucleation times while still generating substantially uniform and substantially contamination-free copper layers with low resistivity and low deposition defects. The longer nucleation times generally enable narrower feature fills.
Furthermore, implementations of the invention described herein provide electroless plating baths that may be used over a wider pH range and temperature range relative to conventional electroless plating baths. As described above, the electroless plating baths described herein may be used within a pH range of pH 10 to pH 12 and a temperature range of 60° C. to 80° C.
The above description of illustrated implementations of the invention, including what is described in the Abstract, is not intended to be exhaustive or to limit the invention to the precise forms disclosed. While specific implementations of, and examples for, the invention are described herein for illustrative purposes, various equivalent modifications are possible within the scope of the invention, as those skilled in the relevant art will recognize.
These modifications may be made to the invention in light of the above detailed description. The terms used in the following claims should not be construed to limit the invention to the specific implementations disclosed in the specification and the claims. Rather, the scope of the invention is to be determined entirely by the following claims, which are to be construed in accordance with established doctrines of claim interpretation.
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