The present disclosure relates generally to an integrated circuit process and more particularly to metal plating.
Some metal plating process for integrated circuit fabrication faces challenges such as slow deposition rate, long plating duration and low wafer per hour (WPH) production. More efficient metal plating apparatus and method with uniform deposition are desirable.
Reference is now made to the following descriptions taken in conjunction with the accompanying drawings, in which:
The making and using of various embodiments are discussed in detail below. It should be appreciated, however, that the present disclosure provides many applicable inventive concepts that can be embodied in a wide variety of specific contexts. The specific embodiments discussed are merely illustrative of specific ways to make and use, and do not limit the scope of the disclosure.
In addition, the present disclosure may repeat reference numerals and/or letters in the various examples. This repetition is for the purpose of simplicity and clarity and does not in itself dictate a relationship between the various embodiments and/or configurations discussed. Moreover, the formation of a feature on, connected to, and/or coupled to another feature in the present disclosure that follows may include embodiments in which the features are formed in direct contact, and may also include embodiments in which additional features may be formed interposing the features, such that the features may not be in direct contact. In addition, spatially relative terms, for example, “lower,” “upper,” “horizontal,” “vertical,” “above,” “over,” “below,” “beneath,” “up,” “down,” “top,” “bottom,” etc. as well as derivatives thereof (e.g., “horizontally,” “downwardly,” “upwardly,” etc.) are used for ease of the present disclosure of one features relationship to another feature. The spatially relative terms are intended to cover different orientations of the device including the features.
Electrolyte such as copper sulphate (CuSO4) solution or any other suitable solution is filled inside the chemical bath chamber 102 for the metal plating process. In some embodiments, the chemical bath chamber 102 has an inner diameter of about 40 cm, an outer diameter of about 45 cm, and a height of about 60 cm. The chemical bath chamber 102 comprises Teflon or any other suitable material and the size can vary depending on applications.
In some embodiments, a wafer being plated functions as the cathode 120 and the plating side of the wafer faces the anode 114. In one example, the anode 114 has a thickness of about 3 cm and comprises copper or any other suitable material.
In some embodiments, a coil frame 104 provides a waterproof enclosure of the solenoid coil 106 within the chemical bath chamber 102. In some embodiments the coil frame 104 has an inner diameter of about 280 mm and an outer diameter of 380 mm, and comprises polyoxymethylene (POM), plastic, silicone, Teflon, any combination thereof, or any other suitable material. One skilled in the art will recognize that the dimensions and diameters provided in this disclosure are for the illustrated embodiments only and will vary according to, e.g., the diameter of the wafers being processed. It is contemplated that as wafer diameters increase, the diameters of the coil frame and other elements will also increase, as may other dimensions disclosed herein.
In some embodiments, the solenoid coil 106 has a diameter of 1.6 mm-2.4 mm, and a wire length of 20 m or more can be wound for the solenoid coil 106. The solenoid coil 106 comprises copper or any other suitable material. In some embodiments, the solenoid coil 106 may have a Teflon coating to isolate and protect it from the electrolyte within the chemical bath chamber 102.
In some embodiments, a metal block 108 enhances the magnetic field B from the solenoid coil 106 and has holes to allow generally uniform movement of the electrolyte in the chemical bath chamber 102 through the holes as shown in
The metal block 108 comprises magnetically conductive material such as metal, e.g., iron, nickel, iron-aluminum alloy, cobalt, low carbon steel, any combination thereof, or any other suitable material. In some embodiments, the metal block 108 may have a Teflon coating to isolate and protect it from the electrolyte within the chemical bath chamber 102. In some embodiments, the permeability of the metal block 108 is at least 100 H/m.
In some embodiments, an anode chamber 110 is disposed within the chemical bath chamber 102 and inside the solenoid coil 106. The anode chamber 110 has a cylinder shape with open ends in
In some embodiments, a mesh cover (membrane) 112 is placed over the anode chamber 110. The mesh cover 112 comprises hydrophilic polyethylene, other synthetic fabric, or any other suitable material. The anode chamber 110 and the mesh cover 112 helps to contain byproducts from copper sludge and/or organic additives during the metal plating process.
The power supply 116 is coupled to the solenoid coil 106 to provide the magnetic field B in the direction from the anode 114 to the cathode 120 (e.g., a wafer). In some embodiments, the voltage of the power supply 116 is 80 V in direct current (DC) or higher, and provides the magnetic field B of 500 gauss (Gs)—600 Gs or higher. The power supply 118 is coupled to the anode 114 and the cathode 120 for the metal plating process. In some embodiments, the voltage of the power supply 118 is 0.1 V-20 V in DC and may be modulated (e.g., pulses). In one example, a waterproof solenoid coil 106 coupled to a 110 V DC power supply 116 and a metal block 108 generates a stable 500 gauss magnetic field from the anode 114 to the cathode 120 in the chemical bath chamber 102.
The metal plating apparatus 100 accelerates metal deposition by applying magnetic field B parallel to the plating current from the anode 114 to the cathode 120 inside the chemical bath chamber 102. The solenoid coil 106 generates paramagnetic force (i.e., magnetic field) and the metal block 108 enhances the magnetic field. The magnetic field increases ion current and improves metal plating deposition rate.
Because the solenoid coil 106 is within the chemical bath chamber 102 and close to the pathway between the anode 114 and the cathode 120, it can generate the magnetic field efficiently in the target area to improve the metal plating rate. In one example, the metal plating apparatus 100 achieved 20% increase in wafer per hour (WPH) production and also improved metal plating uniformity.
In some embodiments, there are multiple holes 202 distributed uniformly over the metal block 108 so that the electrolyte (e.g., CuSO4 solution) can move between the anode 114 and the cathode 120 uniformly in general. It is contemplated that in some embodiments, holes 202 may be distributed non-uniformly over metal block 108; for instance in some embodiments, a non-uniform distribution of holes 202 could be employed to compensate for or otherwise offset a non-uniform distribution of magnetic field B, or to compensate for non-uniform topography or deposition sites on the wafer to which the metal is to be plated, as but examples. The metal block 108 comprises iron, nickel, iron-aluminum alloy, cobalt, low carbon steel, any combination thereof, or any other suitable material. In some embodiments, the permeability of the metal block 108 is at least 100 H/m.
In some embodiments, the metal block 108 is coated with Teflon or any other suitable material so that the metal block 108 is isolated and protected from the electrolyte (e.g., CuSO4 solution) within the metal plating chamber 102.
At step 302, a first power supply voltage is applied to a solenoid coil 106. Thee solenoid coil 106 is disposed within a chemical bath chamber 102 between an anode 114 at a bottom portion of the chemical bath chamber 102 and a cathode 120 (e.g., a wafer) at a top portion of the chemical bath chamber 102.
In some embodiments, a wafer is placed inside the chemical bath chamber 102 and functions as the cathode 120. The plating side of the wafer faces the anode 114. The solenoid coil 106 is arranged to provide a magnetic field B in a direction from the anode 114 to the cathode 120 during the metal plating process. In some embodiments, the first power supply voltage is 80 V in direct current (DC) or higher, and provides the magnetic field B of 500 gauss (Gs)—600 Gs or higher.
At step 304, a second power supply voltage is applied to the anode 114 and the cathode 120 of the chemical bath chamber 102 for the metal plating process. In some embodiments, the second power supply voltage is 0.1 V-20 V in DC.
In various embodiments, a metal block 108 is placed between the anode 114 and the cathode 120. The metal block 108 has at least one hole 202 to allow movement of an electrolyte in the chemical bath chamber 102 through the at least one hole 202. The metal block 108 comprises magnetically conductive material such as metal, e.g., iron, nickel, iron-aluminum alloy, cobalt, low carbon steel, any combination thereof, or any other suitable material. In some embodiments, the metal block 108 may have a Teflon coating to isolate and protect it from the electrolyte within the chemical bath chamber 102. In some embodiments, the permeability of the metal block 108 is at least 100 H/m.
In some embodiments, an anode chamber 110 is disposed within the chemical bath chamber 102 and inside the solenoid coil 106. The anode chamber 110 has a cylinder shape with open ends. The anode chamber 110 has a side wall that surrounds the anode 114 at the bottom portion of the chemical bath chamber 102. The anode chamber 110 comprises polyoxymethylene (POM), plastic, silicone, Teflon, any combination thereof, or any other suitable material.
In some embodiments, a mesh cover (membrane) 112 is placed over the anode chamber 110. In some embodiments, the mesh cover 112 comprises hydrophilic polyethylene, other synthetic fabric, or any other suitable material. The anode chamber 110 and the mesh cover 112 helps to contain byproducts from copper sludge and/or organic additives during the metal plating process.
According to some embodiments, a metal plating apparatus includes a chemical bath chamber, an anode disposed at a bottom portion of the chemical bath chamber, and a cathode disposed at a top portion of the chemical bath chamber. A solenoid coil is disposed within the chemical bath chamber between the anode and the cathode. The solenoid coil is arranged to apply a magnetic field during a metal plating process in a direction from the anode to the cathode.
According to some embodiments, a metal plating method includes applying a first power supply voltage to a solenoid coil. The solenoid coil is disposed within a chemical bath chamber. The solenoid coil is arranged to provide a magnetic field during a metal plating process in a direction from an anode at a bottom portion of the chemical bath chamber to a cathode at a top portion of the chemical bath chamber. A second power supply voltage is applied to the anode and the cathode of the chemical bath chamber for the metal plating process.
A skilled person in the art will appreciate that there can be many embodiment variations of this disclosure. Although the embodiments and their features have been described in detail, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the embodiments. Moreover, the scope of the present application is not intended to be limited to the particular embodiments of the process, machine, manufacture, and composition of matter, means, methods and steps described in the specification. As one of ordinary skill in the art will readily appreciate from the disclosed embodiments, processes, machines, manufacture, compositions of matter, means, methods, or steps, presently existing or later to be developed, that perform substantially the same function or achieve substantially the same result as the corresponding embodiments described herein may be utilized according to the present disclosure.
The above method embodiment shows exemplary steps, but they are not necessarily required to be performed in the order shown. Steps may be added, replaced, changed order, and/or eliminated as appropriate, in accordance with the spirit and scope of embodiment of the disclosure. Embodiments that combine different claims and/or different embodiments are within the scope of the disclosure and will be apparent to those skilled in the art after reviewing this disclosure.
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Number | Date | Country | |
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20140262796 A1 | Sep 2014 | US |