Apparatus and method for controlling plating uniformity

Abstract

The use of an insulating shield for improving the current distribution in an electrochemical plating bath is disclosed. Numerical analysis is used to evaluate the influence of shield shape and position on plating uniformity. Simulation results are compared to experimental data for nickel deposition from a nickel-sulfamate bath. The shield is shown to be an effective and simple way to improve current distribution uniformity, reducing the measured disparity between the average current density and the current density at center of a plating surface center from about 35% to less than about 10%.

Description

TECHNICAL FIELD

[0002] This description of embodiments of an invention generally relates to electroplating systems and more particularly, to an improved shielding apparatus and method to improve the electric field current distribution in electroplating systems.

SUMMARY

[0003] In accordance with one embodiment of the present invention, an electroplating system capable of controlling the thickness of a metal film electrodeposited onto a substrate is provided. The electroplating system includes a standard electroplating apparatus and a non-conductive shield having a certain size and one or more aperture openings, that is disposed in the electroplating apparatus to selectively alter or modulate the electric field between the anode and the plating surface in this embodiment and thereby control the electrodeposition rate across the area of the plating surface.

[0004] The shield is disposed between the anode and the cathode. As a result the electric field is modulated so that a desired time-averaged electric field current-density is applied to every point on the plating surface. Because the electrodeposition rate depends in part on the characteristics of the electric field, the uniformity of the thickness profile of the electrodeposited metal can be manipulated by the size of the shield and of the shield aperture(s).

BRIEF DESCRIPTION OF THE DRAWINGS

[0005] FIG. 1 is a functional block diagram of an electroplating system according to one embodiment of the invention.

[0006] FIGS. 2A and 2B show respectively top views of a first shield having a single central opening and of a second shield having a similar central opening plus a second annular opening concentric to the first opening.

[0007] FIG. 3 shows experimental results and several numerical simulations for electrodeposition onto a 3 inch wafer without the use of a shield.

[0008] FIGS. 4A, 4B, and 4C show experimental and numerical simulation results for the electrodeposited film thickness normalized by the average film thickness on a 3 inch wafer respectively using one of three shields of FIG. 2A, having one of three different aperture sizes, each shield is positioned at a first separation distance above the plating surface.

[0009] FIGS. 5A, 5B, and 5C show experimental and numerical simulation results for the electrodeposited film thickness normalized by the average film thickness on a 3 inch wafer respectively using one of three shields of FIG. 2A having one of the three aperture sizes of FIG. 4, each shield is positioned at a second separation distance above the plating surface.

[0010] FIGS. 6A, 6B, and 6C show experimental and numerical simulation results for the electrodeposited film thickness normalized by the average film thickness on a 3 inch wafer respectively using one of three shields of FIG. 2A each shield positioned at either the second, a third, or a fourth separation distance above the plating surface.

[0011] FIGS. 7A, and 7B show a numerical simulation of current distribution normalized by the average current density at the shield illustrating the influence of the shield radius for the shield designs of FIGS. 2A and 2B, respectively.

[0012] FIGS. FIGS. 8A, and 8B show a numerical simulation of current distribution normalized by the average current density at the shield illustrating the influence of the shield separation distance above the plating surface for the shield designs of FIGS. 2A and 2B, respectively.

[0013] FIGS. 9A, 9B, and 9C show a numerical simulation of current distribution normalized by the average current density at the shield illustrating the influence of three different Wagner numbers using the shield designs of FIGS. 2A (dashed line) and 2B (solid line). Experimentally measured points are shown in FIG. 9B superimposed over the solid and dashed lines.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

[0014] FIG. 1 is a functional block diagram of an electroplating system 100 according to one embodiment of the present invention. The electroplating system 100 includes an anode 102, a cathode 104 and a voltage source (not shown) all contained within an insulating container 120. In addition, electroplating system 100 includes a shield 110 in accordance with the present embodiment and cathode 104 is rotated as indicated at 108 for uniformity.

[0015] This embodiment of electroplating system 100 is adapted for MEMS fabrication and, particularly, for electroplating a semiconductor wafer, with a useful electroplateable metal or alloy such as Cu, Ni, NiFe, NiCo, or FeMn. In the present case, nickel metal was chosen as the anode material for convenience and because of the high Faradic plating efficiency of nickel. The cathode 104 is chosen to be a silicon wafer having a conductive plating surface since this is the standard mold material used for many MEMS and LIGA parts. The reader will appreciate that when reference is made hereinafter to “the substrate”, or to “the wafer,” it is understood that reference is being made to cathode 104 used in the electroplating system 100.

[0016] In the present embodiment, nickel was deposited at 50° C. from a well-mixed solution of 1.54 M Ni(SO3NH2)2 and 0.73 M boric acid. This electrolyte composition is typical for a nickel sulfamate bath used for electroforming. All chemicals were certified ACS grade. Sulfur-depolarized nickel rounds held in a bagged titanium anode basket (Titan International, Inc.) were used as a counter-electrode in a two-electrode arrangement. The pH of the electrolyte was controlled between 3.5 and 4.0, and the average thickness of the nickel film deposited at 15 mA/cm2 was about 100 μm. The conductivity of this solution at 50° C. was measured to be 0.07 S/cm with a conductivity meter (Corning). Plating substrates were 3 inch diameter silicon wafers (˜650 μm thick) with a copper metallization layer serving as a conductive plating base.

[0017] The arrangement of the cell is shown in FIG. 1. A 10 liter cylindrical glass jar was used as the electroplating system container 120 of the present embodiment but any non-conducting container having reasonable dimensions could also be used. In particular, the container may be generally rectilinear. Furthermore, the electrodes and plating surface(s) need not be circular but may be also rectilinear so long as the size and shape of each is chosen to avoid generating large gradients within the electric field in the cell bath.

[0018] Silicon wafer 104 was taped down to a plastic support fixture 106 comprising poly(methyl methacrylate) (e.g., Plexiglas®, Lucite®) with insulating plating tape. Electrical contact was made to the wafer by running a strip of copper tape from the top of support 106 down to the wafer 104 and then to one pole the power supply (not shown). The exposed surfaces of the copper strip were masked with insulating tape to avoid perturbing the cell electric field when the cell was in use. Finally, insulating shield 110 (again, Plexiglas®, or Lucite®) was put in place over the wafer 104 and between it and anode 102 as shown in FIG. 1.

[0019] Wafers were weighed before and after electrodeposition to determine the average thickness of the nickel film that was eventually deposited during plating. In all cases the measured mass of nickel compared well with that which would be expected via Faraday's law (as ready mentioned the Faradic efficiency for nickel deposition is high; deposition from a sulfamate bath is known to closely approach 100%.). Nickel thickness as a function of the radial position across the surface 105 of wafer 104 was determined with a point micrometer (accurate to ±1 μm) by subtracting the initial wafer thickness from the total measured height of the plated wafer (metallized substrate and plated nickel film). To ensure that only substantially flat wafers were used, the thickness of each wafer (including the thin copper layer) was measured at several points across the surface and compare to a reference standard before deposition. Moreover, because the thickness and stiffness of the silicon wafer is several orders of magnitude greater than the deposited nickel film no “bowing” of the wafer was expected during post-processing measurements. All of the reported values are the average of measurements across at least 5 different radii from two different wafers.

[0020] In this particular embodiment, while anode 102 is shown in FIG. 1 as disc shaped it in fact, comprises a plurality of individual nickel bodies and the cathode 104 have generally the same diameter and are relatively disposed in an electrolytic solution so that the anode 102 and the cathode 104 are parallel and are separated by certain distance dependent upon the wafer diameter and aligned about coaxially. In the present embodiments using the 3 inch Ø wafer the separation distance is about 6 inches or about twice the diameter of the wafer. In addition, the anode 102 and cathode 104. Although separated by a generally large distance other electrode configurations are possible including a close-coupled electrode configuration, a remote or virtual anode configuration, and anodes that have a size and shape different then the size and shape of the cathode.

[0021] A voltage source (not shown) is connected to the anode 102 and the cathode 104 to set up an electric field between the anode 102 and the cathode 104, as indicated by gradient lines 112. In general, any suitable commercially available or custom electroplating apparatus with a mechanism for rotating the plating surface can be used for this embodiment of the invention. Moreover, any standard power supply capable of operating in constant current/constant potential can be used. In the present case, an Agilent® 6552A system available Agilent Technologies, Inc., was used to provide a constant current source.

[0022] In accordance with this embodiment of the invention, the shield 110 is disposed between anode 102 and the cathode 104 to selectively vary or modulate the time-averaged intensity of the electric field 112 between the anode 102 and the cathode 104. In this embodiment, the shield 110 is located about ¾ inch from the cathode 104, but the position of the shield 110 can range from ¾ inch to about 1½ inches anode 102 depending upon various parameters of the shield itself.

[0023] The shield 110 is preferably made of a non-conductive material that is resistant to the acid bath typically used in nickel electroplating processes. For example, the shield 110 can be made of polyethylene, polypropylene, fluoropolymers (e.g., Teflon®, or polyvinylidene fluoride (PVDF). A mechanical bracket or collar can be used to position the shield 110 in the electroplating cell as desired. Thus, the shield 110 can be easily removed or modified as required and, further, can be easily retrofitted to existing electroplating apparatus.

[0024] Shield 110 comprises one of two configuration shown in FIGS. 2A and 2B.

[0025] The shield 110 is shaped so that, in conjunction with the rotation of cathode 104 and the location of the shield's between the two electrodes, the time-averaged electric field 112 present between anode 102 and any particular point on the cathode plating surface 105 is controlled. Moreover, because the electric field is controlled the local electrodeposition rate of nickel across the plating surface 105 is also controlled.

[0026] FIG. 1 illustrates a cartoon of the experimental electrodeposition cell of the present embodiment showing many characteristic cell parameters and their relationship to one another. Table 1 below provides a summary of the cell parameter. (Parameters that are “normalized” were done so by comparing each a standard wafer radius ro of 38 mm.)

[0027] Throughout the remainder of the description, most of these parameters are dealt with as “dimensionless” by setting each as a ratio of the standard wafer radius ro of 38 mm, i.e., each parameter is “normalized” with respect to the wafer radius. In particular, the wafer holder thickness and diameter were set to 0.08 and 2 respectively. Moreover, the wafer thickness is 0.02 for all wafers in the present study.

TABLE 1
VARIABLE VALUE
αc       0.5
h        ˜0.75 cm to ˜2 cm
κ        0.07 Ω−1 cm−1
ri       2.57 cm
rho      ˜1.3 cm to ˜2.5 cm
ro       3.8 cm
rs       ˜7.6 cm to˜12.16 cm
rt       2.76 cm
iavg     15 mA/cm2
WaT      0 to˜1

Mathematical Model

[0028] A mathematical model was developed to provide insight as to which parameters are most influential for uniform deposition and against which our experimental results might by compared. It is assumed that the electrolyte bath is well mixed and that any variation in ion concentration throughout the bath is negligible. As such, the current density i, is determined by the gradient of the electrical potential φ.

i =−κ{overscore (∇)}φ  (1)

[0029] where the electrolyte conductivity κ is presumed to be constant. The potential field is then determined by Laplace's equation, which for the present case is most conveniently written in cylindrical coordinates as: 1$\begin{array}{cc}\frac{{\partial }^2\phi }{\partial r^2}+\frac{1}{r}\frac{\partial \phi }{\partial r}+\frac{{\partial }^2\phi }{\partial z^2}=0& \left(2\right)\end{array}$

[0030] Along the insulating wafer holder, the current shield, and all insulating walls, the normal component of the electrical potential gradient is zero, i.e.,

{overscore (n)}·{overscore (∇)}φ= 0  (3)

[0031] where {overscore (n)} is the unit vector normal to the surface. Moreover, the boundary condition along the counter-electrode is assumed to be an imposed uniform current density: 2$\begin{array}{cc}\left(\stackrel{\_}{n}·\stackrel{\_}{\nabla }\phi \right)=-\frac{i_{\mathrm{avg}}}{\kappa }& \left(4\right)\end{array}$

[0032] where iavg is an average current density on the cathode. Because the counter-electrode position was sufficiently removed from cathode surface 105, the boundary condition represented by equation (4) had an insignificant influence on the results. Employment of equation 4 is a computationally convenient method of setting the total current flowing in the electrochemical cell.

[0033] At cathode surface 105, a Tafel kinetics relationship is assumed: 3$\begin{array}{cc}\begin{array}{cc}\frac{\partial \phi }{\partial z}=-\frac{i_o}{\kappa }\exp \left(-\frac{{\alpha }_{c}F\left(V-\phi \right)}{\mathrm{RT}}\right)& \mathrm{at}z=0,r\le r_o\end{array}& \left(5\right)\end{array}$

[0034] where αc is the cathodic charge transfer coefficient.

[0035] The numerical calculations were performed by well known boundary element methods previously described in the literature (see for instance Radek Chalupa, Yang Cao, and Alan C. West, “Unsteady Diffusion Effects in Electrodeposition in Submicron Features,” Journal of Applied Electrochemistry, v.32, p135 (2002); and Yang Cao, Premratn Taephaisitphongse, Radek Chalupa, Alan C. West, “A Three-Additive Model of Superfilling of Copper,” Journal of the Electrochemical Society, v.148, (7) pp. C466-C472 (2001), both herein incorporated by reference) and validated. The node density was systematically varied to ensure that the numerical error associated with the grid was less than approximately 2 percent. Further grid refinements to achieve greater accuracy was not required for the present purpose of obtaining an optimal shield design.

[0036] Results depend on several ratios of the cell dimensions as well as a Tafel Wagner number defined as: 4$\begin{array}{cc}{W}_{a_T}=\frac{\kappa \mathrm{RT}}{\&LeftBracketingBar;i_{\mathrm{avg}}\&RightBracketingBar;{\alpha }_c{r}_{o}F}& \left(6\right)\end{array}$

[0037] FIG. 2 shows the calculated current distribution for several Wagner numbers that would result when a shield is not employed. As expected, the computed current distributions become more uniform as the Wagner number increases. For the case of WaT=0.07, experimental results are also shown and are in good agreement with simulation, as is readily seen.

[0038] As suggested by the range of the parameters listed in TABLE 1, only the dimensions of overall shield radius and aperture radius were systematically varied in the present investigation. The dimensionless shield thickness was found not to be an important parameter, and its value was set at 0.08. Furthermore, for most of the experimental results reported here iavg=15 mA/cm2, κ=0.07 Ω−1cm−1, ro=3.8 cm so as to provide a Tafel-Wagner number of WaT=0.07.

[0039] As one might expect, the parameters found to be of most significance to the present study are the ratio of aperture radius to the wafer radius rho/ro; the separation distance between the shield and wafer (normalized to wafer radius) h/ro; and the ratio of shield radius to the wafer radius rs/ro.

[0040] FIGS. 3A-C and 4A-C show the effect on deposition thickness when using shields (design A) having one of three different aperture sizes rho/ro; at separation distances h/ro, of 0.25 (FIG. 3) and of 0.28 (FIG. 4), respectively (WaT=0.07 and rs/ro=2). In each case the experimental measurements were found to be in good agreement with the numerical simulations. Moreover, as suggested by FIGS. 3A and 4A (rho/ro;=0.34), as the aperture size is made smaller, the film thickness t, near the wafer center becomes unacceptably large. Furthermore, for aperture sizes rho/ro>0.7 (results not shown), film thickness t, begins to approximate the results of FIG. 2 for the case of no shield.

[0041] FIGS. 5A-5C shows the influence of shield separation distance h/ro, over a fairly narrow range for the case of rho/ro=0.5, again with WaT=0.07, and rs/ro=2. It is seen from these results that as the separation distance is reduced to h/ro<0.2, the thickness distribution becomes significantly altered near the wafer center as compared to the example of FIGS. 3C (h/ro=0.25). Furthermore, setting h/ro between about 0.25 and about 0.34, provides much less variation in film thickness across the wafer surface. However, as with too large an aperture size, numerical simulation indicates that when separation distance exceeds about 0.7, film thickness deposition approaches what would be expected for the no-shield case.

[0042] Results shown in FIGS. 3-5 (numerical simulation and experimental), therefore, suggest that there is an optimal shield separation distance and aperture radius. Additionally, simulation results showing the influence of the overall shield radius rs/ro as presented in FIGS. 6A and 6B, suggests that current distribution near the wafer center increases as the size of the shield increases, and that for each shield size the current distribution reaches a minimum near r/ro=0.7 further suggesting that a shield, designed with a second opening, concentric with the central aperture, might moderate the observed minimum in the current (and therefore, deposition) profile. The numerical simulations shown in FIGS. 6B and 7B demonstrate that for the case in which the midpoint of the annular opening is centered at about rs/ro=0.7 current distribution could be improve.

[0043] Based on these simulation results, shield design B, shown in FIG. 2B, was constructed. The modified design comprises a shield with a narrow annular opening surrounding the central aperture wherein the inside edge of the annular opening ri/ro is scaled to be equal to 0.675, and the outside edge of the opening rt/ro is equal to 0.725 with several small bridging elements connecting the inner aperture to the body of the shield.

[0044] Simulation and experimental data shown in FIGS. 8A-8C compares the effect the shield design change on current distribution for three different Tafel-Wagner numbers. Dashed lines represent the current distribution in a cell designed with shield A and assume that rho/ro=0.5, h/ro=0.34, and rs/ro=2. Solid lines show the current distribution for a cell designed with shield B (rt/ro=0.675 and rt/ro=0.725), and assume that rho/ro=0.5, h/ro=0.34, and rs/ro=3.2.

[0045] The effect of the shield modification on measured current distribution is shown in FIGS. 8B for a Tafel-Wagner number of 0.07 and is seen to closely track the simulation data of shield design B. Moreover, these results strongly suggest that current distribution in cells using the modified shield (B) will be more uniform than in cells that use the un-modified shield (A): using a shield with a central aperture reduces the maximum deviation in the current distribution by about 20% of its average near the cathode center (for r/ro≦0.7), while an improved design implementing a slot appropriately placed around the aperture reduces the variation to less than about 10% of its average (again, for r/ro≦0.7).

Claims

1. An intermediate member for modifying an electric field in an electrochemical plating cell, comprising: an electrically nonconducting disc disposed between an anode and a cathode and about parallel to said cathode, said disc comprising a central aperture having a radius rap, said central aperture disposed about coaxially with a center line normal to said cathode.

2. The intermediate member of claim 1, wherein said cathode comprises a radius rc, and said electrically nonconducting disc further comprises a radius rd, wherein said radius rd is at least as large as said cathode radius rc.

3. The intermediate member of claim 2, wherein said central aperture radius rap is greater then about 0.5rc and less then 0.7rc.

4. The intermediate member of claim 2, wherein said radius rd is equal to between about rc and about 2rc.

5. The intermediate member of claim 3, wherein rap is equal to about 0.66rc.

6. The intermediate member of claim 1, wherein the electrically nonconducting disc comprises a mechanically stable material compatible with a acidic liquid environment.

7. The intermediate member of claim 6, wherein the electrically nonconducting disc is selected from the group of materials consisting of polyethylene, polypropylene, and fluoropolymers.

8. An intermediate member for modifying an electric field in an electrochemical plating cell, comprising: an electrically nonconducting disc disposed between an anode and a cathode and about parallel to said cathode, said disc comprising a central aperture having a radius rap, and a segmented annular opening having an opening width whose midpoint has a radius of rao concentric to said central aperture, said central aperture disposed about coaxially with a center line normal to said cathode.

9. The intermediate member of claim 8, wherein said cathode comprises a radius rc, and said electrically nonconducting disc further comprises a radius rd, wherein said radius rd is at least as large as said cathode radius rc.

10. The intermediate member of claim 9, wherein said central aperture radius rap is greater then about 0.5rc and less then 0.7rc.

11. The intermediate member of claim 8, wherein said radius rd is equal to between about rc and about 2rc.

12. The intermediate member of claim 8, wherein rap is equal to about 0.66rc.

13. The intermediate member of claim 8, wherein the electrically nonconducting disc comprises a mechanically stable material compatible with a acidic liquid environment.

14. The intermediate member of claim 13, wherein the electrically nonconducting disc is selected from the group of materials consisting of polyethylene, polypropylene, and fluoropolymers.

15. The intermediate member of claim 8, wherein said segmented annular opening comprises an inner radius ri and an outer radius rt, wherein

16. The intermediate member of claim 15, wherein (rt−ri)≅0.05rc.

17. An electrochemical plating system, comprising: an electrically nonconducting disc disposed between an anode and a cathode and about parallel to said cathode, said disc comprising a central aperture having a radius rap, and a segmented annular opening having an opening width whose midpoint has a radius of rao concentric to said central aperture, said central aperture disposed about coaxially with a center line normal to said cathode.

18. The electrochemical system of claim 17, wherein said cathode comprises a radius rc, and said electrically nonconducting disc further comprises a radius rd, wherein said radius rd is at least as large as said cathode radius rc, said disc further disposed at a distance from said cathode equal to about 0.34rc to less then about 0.5rc.

19. The electrochemical system of claim 18, wherein said radius rd is equal to between about rc and about 2rc.

20. The electrochemical system of claim 19, wherein rap is equal to about 0.66rc.

21. The electrochemical system of claim 17, wherein the electrically nonconducting disc comprises a mechanically stable material compatible with a acidic liquid environment.

22. The electrochemical system of claim 20, wherein the electrically nonconducting disc is selected from the group of materials consisting of polyethylene, polypropylene, and fluoropolymers.

23. The electrochemical system of claim 18, wherein said segmented annular opening comprises an inner radius ri and an outer radius rt, wherein

24. The electrochemical system of claim 23, wherein (rt−ri)≅0.05rc.

25. A method for increasing plating deposition uniformity across a plating surface in an electrochemical plating system, comprising the step of: disposing an electrically nonconducting shield disposed between an anode and a cathode in said electrochemical plating system, said shield comprising a central aperture having a radius rap, and a segmented annular opening having an opening width whose midpoint has a radius of rao concentric to said central aperture; orienting said shield about parallel to said cathode and said central aperture about coaxially with a center line normal to said cathode; and setting said shield at a distance from said cathode equal to about 0.34rc to less then about 0.5rc.