Patent Application
20080032606
Pursuant to 35 U.S.C. § 119 and the Paris Convention Treaty, this application claims the benefit of Chinese Patent Application No. 200610014300.0 filed Jun. 9, 2006, the contents of which are incorporated herein by reference.
1. Technical Field
This invention relates to a chemical-mechanical planarization technique, especially designed to control the dishing problem arising during the manufacture of copper multilayer interconnection structures in ultra large-scale integrated circuits.
2. Background of the Invention
As the integrated circuit density increases and the device feature size becomes smaller, the electrical resistance and capacitance of the metal are enhanced, which causes the interconnect delay time RC to increase and, hence, decreases the speed of the circuitry (R and C refer to metal wire resistance, and interlevel dielectric capacitance, respectively).
Because copper has higher resistance to electromigration, and lower resistivity and heat sensitivity than aluminum, it can reduce the RC delay time and raise circuital reliability. This characteristic makes it a good candidate for multilayer interconnections. However, the adhesion ability between copper and the dielectric layer is unstable, and copper easily diffuses into substances such as silicon and silicon dioxide, forming a deep energy level in these substances, which adversely affects the power characteristics of components.
To successfully accomplish copper metallization on silicon chips, barrier films need to be used to limit the mutual diffusion between copper and silicon. The Damascene process, which uses copper-CMP (Cu-CMP), is a mature technology that has been successfully applied for conductor patterning in integrated circuit manufacture. For getting an accurate photoetch pattern and optimum electrical properties in multilayer interconnection structures, the key to achieving success is to guarantee a global planarization of each level. Cu-CMP serves to remove the copper and the barrier layer to the top level of the insulating layer. At the same time, global and local planarization of the copper surface is realized.
The dishing problem, i.e., a polishing non-uniformity, occurring during Cu-CMP of multilayer interconnection structures in ULSI results in increased electrical noise, lack of uniform electrical characteristics, increased RC delay time, and has adverse effects on integration, reliability, and cost.
Because copper, tantalum, and the dielectric layer have different physical and chemical properties, if a single polishing slurry and polishing conditions are used for Cu-CMP, the polishing speeds will be different and the selection ratio will not be ideal for all substrates. Specifically, copper has a faster polish speed than the barrier layer material and the dielectric layer, contributing to the dishing problem during CMP and often bringing about a short circuit with catastrophic consequences.
Currently, the dishing problem is the most difficult challenge in Cu-CMP. Conventional Cu-CMP processes include the use of acidic slurries, followed by strong mechanical lapping, followed by additional applications of acidic slurries. However, the barrier layer (e.g., Ta, TaN, TiN) and the dielectric layer are more stable to acid than is copper, and if the above-mentioned method is employed, the polishing speeds of the barrier layer and the dielectric layer are too low, and the dishing problem is difficult to solve.
Cu-CMP polishing slurries can be divided into two major categories according to their pH value: acidic and alkaline. Conventionally acidic slurries have been used for Cu-CMP because acids easily dissolve copper. For example, nitric acid has been widely used in the process, as it easily reacts with copper to yield soluble cupric nitrate according to the following chemical equation:
3 Cu+8 HNO3 (dilute)→3 Cu(NO3)2+2 NO+4 H2O.
However, using nitric acid results in a poor selectivity between high and low spots, i.e., the removal speed at different locations of the surface is almost the same, making it difficult to achieve global planarization.
Chinese Patent No. CN1312845 calls for addition of benzotriazole (BTA) to an acid slurry to control dishing. The BTA reacts with copper and produces a Cu-BTA monolayer which can restrain the reaction of nitric acid with copper. Thus, the inner copper layer is not corrupted, the polishing speeds of the bulgy and concave copper surfaces are different, and as a result, planarization is achieved. However, it is difficult to achieve a high process speed when using BTA, and the speed attained is only about 70% of the speed that can be attained when BTA is not used.
When acidic polishing slurry is used, it is difficult to form a stable copper complex, and conversely it is easy to cause cupric ion pollution. In addition, the use of acidic slurry degrades the polishing equipment very rapidly. Finally, environmental pollution resulting from the use of the acidic slurry is a major concern, as is the operator's health. Conventional Cu-CMP processes also utilize EDTA or its disodium salt as the chelating agent. However, EDTA does not dissolve in water at low pHs, and its water-soluble disodium salt leads to metal ion contamination. Accordingly, much opportunity remains for improvement in the area of Cu-CMP.
In one aspect of this invention provided is a solution to the dishing problem. Specifically, a control method for the dishing problem arising during chemical mechanical polishing of copper multilayer interconnection in ULSI is provided.
In certain embodiments of the invention, the Cu-CMP features strong complexation, strong chemical action, no scratching, and low cost.
In certain embodiments of the invention, the polishing slurry comprises: SiO2 hydrosol having different amounts of deionized water as the abrasive; a chelating agent that can chelate the metal ion at pH levels from 9.5 to 11.5; nonionic surfactant(s); and oxidizing agent(s).
In certain embodiments of the invention, the flow speed of the slurry is 200-5000 ml/min, the temperature is 20-40° C., the rotation speed of the polishing pads is 60-120 rpm, the pressure is 100-250 g/cm2, and the polishing speed is 200-1100 nm/min. Under these conditions, the process involves 1-5 min of polishing the copper layer, followed by 30-60 sec of polishing the copper, the barrier layer, and the dielectric layer.
In certain embodiments of the invention, the abrasive is SiO2 hydrosol having particle diameters ranging from 15-40 nm, and starting concentration ranging from 20-50 wt. %. This means that for each 100 g of undiluted SiO2 hydrosol there is from 20 to 50 g of SiO2 particles. The SiO2 hydrosol is then further diluted with deionized water when the CMP slurry is prepared. The weight proportion between the abrasive and the added deionized water is from 1:1 to 1:5.
In certain embodiments of the invention, the metal ion chelating agent is a compound which can form a large-membered chelating ring with metal ions. Particularly, the metal ion chelating agent is a salt of EDTA with a 1,2-diaminoalkan(poly)ol. More particularly, the metal ion chelating agent is an EDTA salt formed with 4 equivalents of 3,4-diaminobutane-1,1,2,2-tetraol, also referred to herein as EDTA·4 3,4-diaminobutane-1,1,2,2-tetraol. In certain embodiments, the metal ion chelating agent is water soluble and assists in oxidation.
Under alkaline conditions, EDTA·4 3,4-diaminobutane-1,1,2,2-tetraol has a stable chelating effect on several different metals, and experimental results indicate that it reacts with metal ions yielding a water soluble complex. The volume percentage of a chelating agent is about 0.5-10% with respect to the volume of the slurry.
In certain embodiments of the invention, the nonionic surfactant is an alcohol ether surfactant, such as a fatty amine oxide (FA/O) surfactant, a JFC surfactant, a fatty alcohol ethoxylate (AEO) surfactant, a fatty amine ethoxylate surfactant, fatty alkanolamide surfactant, or derivatives thereof. The volume percentage of a nonionic surfactant is about 0.5-10% with respect to the volume of the slurry.
In certain embodiments of the invention, the oxidizing agent is an oxide, particularly a peroxide, and more particularly hydrogen peroxide (H2O2). The volume percentage of the oxidizing agent is 0.5-10% with respect to the volume of the slurry.
Below, the invention is explained in more detail with reference to accompanying drawings, in which:
Cu-CMP according to the invention is conducted under high pressure, high-speed rotation of polishing pads, and alkaline conditions promoting strong complexation. Under these conditions, the barrier metal to be removed is transformed into a water-soluble complex, and the dielectric layer to be removed is transformed into an amine salt, which is water soluble. The materials that conventionally have a fast removal speed (such as copper) are converted into compounds that are difficult to dissolve in water. Without wishing to be bound by theory, this principle may be directly responsible for providing solution to the dishing problem.
Cu-CMP is performed under alkali condition, uses SiO2 as the abrasive having particle diameters ranging from 15-40 nm, uses a surfactant and a chelating agent, and the pH is maintained in the range of 9.5-11.5.
The surfactant is an FA/O surfactant a polyoxyethylene ether surfactant, a non-ionic surfactant, or any other suitable surfactant. The FA/O surfactant is, for example, an alkyl phenol ethoxylate of the general Formula I, wherein R is an alkyl, and n is an integer greater than about 5; more particularly, R is an alkyl having at least 6 carbon atoms, and n is an integer from 7 to 10; and most particularly, R is a decyl and n is equal to 7 or 10.
The polyoxyethylene ether surfactant is, for example, a fatty alcohol polyoxyethylene ether of the general Formula II, wherein R is an alkyl, and n is an integer greater than about 5; more particularly, R is an alkyl having at least 6 carbon atoms, and n is an integer from 10 to 25; and most particularly, R is a straight chain alkyl having from twelve to eighteen carbon atoms, and n is 15 or 20.
The chelating agent is, e.g., a water-soluble FA/O chelating agent. Particularly, EDTA·4 3,4-diaminobutane-1,1,2,2-tetraol of Formula III
is used as a chelating agent. EDTA·4 3,4-diaminobutane-1,1,2,2-tetraol is a potent chelator for many metal ions, and it acts simultaneously as a buffer and an antioxidant. It is also relatively inexpensive.
Under certain process conditions, consistent polishing speeds of the copper, the barrier layer, and the dielectric layer are realized which effectively reduces the dishing problem, reduces cross-contamination of surfaces, and meets the needs of successful copper interconnections in the industry. The methods described herein can obtain near-perfect surface smoothness.
The method according to this invention uses an alkaline slurry that can achieve planarization of interconnections, high smoothness, good selectivity, low scratching, higher polishing speeds, effective control of metal ion contamination, lower concentration as compared with acid slurry, easy clean-up, and low environmental pollution.
Without wishing to be bound by theory, the following is a model mechanism of alkaline slurry for Cu-CMP:
The method according to this invention utilizes metal complexation under alkaline conditions. At these conditions, the chelating agent has a strong complexing action with respect to Cu, Ta barrier material, SiO2 dielectric layer material, and the tungsten interlayer plug. The resultant complex, or the amine salt, is easily soluble in water, which improves the polishing speed. Under optimal conditions, it is possible to consistently achieve high polishing speeds for different materials, which helps to control the dishing pit appearance, as shown in
The method according to this invention achieves high polishing speeds for copper, tantalum, and the dielectric layer, with polishing speeds in the range of 200-1100 nm/min. With reference to
The invention will now be described in more detail with respect to the following, specific, non-limiting examples.
In order to resolve the dishing pit problem, the copper wire CMP process can be divided into two steps, which are initial polishing and final polishing. The following abbreviations are used: FA/O I surfactant: compound of Formula I,
wherein R is a decyl and n is equal to 7; FA/O chelating agent: compound of Formula III,
The compound of Formula III has been purchased from Tianjin Jingling Microelectronic Materials Limited Company and was sold under the brand name FA/O II chelating agent.
The polishing slurry and the polishing condition of the initial polishing and the final polishing are as follows.
For the initial polishing stage of Cu-CMP, the slurry characteristics are as follows: the SiO2 sol abrasive size is 40 nm, the SiO2 initial concentration is 40 wt. %, the proportion of SiO2 abrasive to deionized water is 1:1, the FA/O I surfactant concentration is 50 ml/L of the slurry, the FA/O chelating agent concentration is 50 ml/L of the slurry, the pH ranges from 9.5-11.5, and the oxidant H2O2 concentration is 30 ml/L of the slurry. The polishing condition: pressure is 200 g/cm2, the slurry flow is 200 ml/min, the rotation speed is 100 rpm, the temperature is 30° C., the polishing speed ranges between 200-1100 nm/min, and the polishing time is 1-5 min. The initial polishing speeds are exemplified in Table 1.
The copper polishing speed is relatively high during the initial polishing, where it can reach above 700 nm/min, which is higher than in systems employed by Fujimi, Rodel, Cabot, and DuPont (500-600 nm/min).
When approaching the end point of the copper layer, i.e., near to the barrier metal and the dielectric layer material, the polishing speed of the barrier material and the SiO2 medium is relatively low, and the selection ratio of copper vs. tantalum and medium is relatively high (>20:1), which is suitable for production applications.
For the final polishing stage of Cu-CMP, the slurry characteristics are as follows: the SiO2 sol abrasive particle size is 15 nm, the initial SiO2 concentration is 40 wt. %, the proportion of SiO2 abrasive to deionized water is 1:2, the FA/O I surfactant concentration is 50 ml/L of the slurry, the FA/O chelating agent concentration is 100 ml/L of the slurry, the pH ranges from 9.5 to 11.5, and the oxidant H2O2 concentration is 5 ml/L of the slurry. The polishing conditions are as follows: the pressure is 100 g/cm2, the slurry flow is 4000 ml/min, the rotation speed is 60 rpm, the temperature is 25° C., the polishing speed ranges between 200-1100 nm/min, and the polishing time is 30-60 sec. The final polishing speeds are exemplified in Table 2.
During the final polishing, the tantalum polishing speed can exceed 700 nm/min. The polishing speed of the copper layer, the Ta barrier layer, and the SiO2 dielectric layer are in substantial agreement, and selection ratio of copper, tantalum, and the SiO2 medium is 1:1:1. The speed can be controlled according to the actual production requirements, and the dishing problem is controlled effectively.
The polishing slurry and the polishing condition of the initial polishing and the final polishing are as follows.
For the initial polishing stage of Cu-CMP, the slurry characteristics are as follows: the SiO2 sol abrasive particle size is 20 nm, the initial SiO2 concentration is 50 wt. %, the proportion of the SiO2 abrasive to deionized water is 1:3, the FA/O I surfactant concentration is 80 ml/L of the slurry, the FA/O chelating agent concentration is 60 ml/L of the slurry, the pH is in the range from about 9.5 to about 11.5, and the oxidant H2O2 concentration is 30 ml/L of the slurry. The polishing conditions are as follows: the polishing pressure is 250 g/cm2, the slurry flow is 200 ml/min, the rotation speed is 120 rpm, the temperature is 40° C., and the polishing time is 1-5 min.
For the final polishing stage of Cu-CMP, the slurry characteristics are as follows: the SiO2 sol abrasive particle size is15 nm, the initial SiO2 concentration is 40 wt. %, the proportion of the SiO2 abrasive to deionized water is 1:2, the FA/O I surfactant concentration is 50 ml/L of the slurry, the FA/O chelating agent concentration is 100 ml/L of the slurry, the pH is in the range of from about 9.5 to about 11.5, and the oxidant H2O2 concentration is 15 ml/L of the slurry. The polishing conditions are: the pressure is 150 g/cm2, the slurry flow is 2000 ml/min, the rotation speed is 80 rpm, the temperature is 20° C., and the polishing time is 30-60 sec. All other conditions are the same as in Example 1.
This invention is not to be limited to the specific embodiments disclosed herein and modifications for various applications and other embodiments are intended to be included within the scope of the appended claims. While this invention has been described in connection with particular examples thereof, the true scope of the invention should not be so limited since other modifications will become apparent to the skilled practitioner upon a study of the drawings, specification, and following claims.
All publications and patent applications mentioned in this specification are indicative of the level of skill of those skilled in the art to which this invention pertains. All publications and patent applications mentioned in this specification are herein incorporated by reference to the same extent as if each individual publication or patent application mentioned in this specification was specifically and individually indicated to be incorporated by reference.
| Number | Date | Country | Kind |
|---|---|---|---|
| 200610014300.0 | Jun 2006 | CN | national |
