WO2006086169A2 - Immersion process for electroplating applications - Google Patents

Immersion process for electroplating applications Download PDF

Info

Publication number
WO2006086169A2
WO2006086169A2 PCT/US2006/003025 US2006003025W WO2006086169A2 WO 2006086169 A2 WO2006086169 A2 WO 2006086169A2 US 2006003025 W US2006003025 W US 2006003025W WO 2006086169 A2 WO2006086169 A2 WO 2006086169A2
Authority
WO
WIPO (PCT)
Prior art keywords
substrate
waveform
plating
current
applying
Prior art date
Application number
PCT/US2006/003025
Other languages
French (fr)
Other versions
WO2006086169A3 (en
Inventor
Hooman Hafezi
Joseph Behnke
Aron Rosenfeld
Timothy R. Webb
Joseph Yahalom
Christopher Reiss Mcguirk
Original Assignee
Applied Materials, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Applied Materials, Inc. filed Critical Applied Materials, Inc.
Publication of WO2006086169A2 publication Critical patent/WO2006086169A2/en
Publication of WO2006086169A3 publication Critical patent/WO2006086169A3/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/18Electroplating using modulated, pulsed or reversing current
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/34Pretreatment of metallic surfaces to be electroplated
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D7/00Electroplating characterised by the article coated
    • C25D7/12Semiconductors
    • C25D7/123Semiconductors first coated with a seed layer or a conductive layer
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/04Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer
    • H01L21/18Manufacture or treatment of semiconductor devices or of parts thereof the devices having at least one potential-jump barrier or surface barrier, e.g. PN junction, depletion layer or carrier concentration layer the devices having semiconductor bodies comprising elements of Group IV of the Periodic System or AIIIBV compounds with or without impurities, e.g. doping materials
    • H01L21/28Manufacture of electrodes on semiconductor bodies using processes or apparatus not provided for in groups H01L21/20 - H01L21/268
    • H01L21/283Deposition of conductive or insulating materials for electrodes conducting electric current
    • H01L21/288Deposition of conductive or insulating materials for electrodes conducting electric current from a liquid, e.g. electrolytic deposition
    • H01L21/2885Deposition of conductive or insulating materials for electrodes conducting electric current from a liquid, e.g. electrolytic deposition using an external electrical current, i.e. electro-deposition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01LSEMICONDUCTOR DEVICES NOT COVERED BY CLASS H10
    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/70Manufacture or treatment of devices consisting of a plurality of solid state components formed in or on a common substrate or of parts thereof; Manufacture of integrated circuit devices or of parts thereof
    • H01L21/71Manufacture of specific parts of devices defined in group H01L21/70
    • H01L21/768Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics
    • H01L21/76838Applying interconnections to be used for carrying current between separate components within a device comprising conductors and dielectrics characterised by the formation and the after-treatment of the conductors
    • H01L21/76877Filling of holes, grooves or trenches, e.g. vias, with conductive material

Definitions

  • the application of the electrical bias causes the metal source to be plated onto the biased seed layer, thus depositing a layer of the ions on the substrate surface that fills the features.
  • the plating solutions which are generally acidic, may chemically etch the seed layer during the process of immersing the substrate in the plating solution.
  • the chemical etching that may take place during the immersion process may result in conductive discontinuities in the seed layer, which may cause plating irregularities in the subsequent plating processes. Therefore, in order to prevent chemical etching during the immersion process, conventional electroplating systems apply an electrical loading bias to the substrate seed layer during the immersion process.
  • the loading bias is generally configured to apply a cathodic bias to the substrate in order to prevent the chemical etching process and to cause at least some forward plating to occur.
  • the loading bias is a constant voltage applied to the substrate as the substrate is immersed in the plating solution and is maintained until the wafer reaches its plating position.
  • the loading bias must be high enough to protect the seed layer from chemical etching and is in many cases higher for thinner seeds. In general, smaller features require thinner seeds. Therefore, as features become smaller, the required loading bias increases. It may also be desirable to further increase the loading bias beyond the level required to protect the seed layer in order to enhance nucleation of the electrodeposit.
  • the conventional process is subject to failure for a number of problems.
  • the loading bias applied during the immersion may fill small features if it is sustained until the plating position is reached.
  • this can lead to the formation of undesirable pinch-off voids.
  • a pinch-off void is typically created when the current density on the sidewalls of a feature is high enough compared to the current density at the bottom of the feature such that the feature opening closes before the feature is fully filled.
  • One or more embodiments of the present invention are generally directed to a method for immersing a substrate into a plating solution.
  • the method includes applying a first waveform to the substrate as the substrate is being immersed into the plating solution, stopping the application of the first waveform to the substrate as soon as the substrate is fully immersed inside the plating solution, and applying a second waveform to the substrate prior to the substrate being situated into a plating position.
  • Figure 1 illustrates a plating cell that may be used in connection with one or more embodiments of the invention.
  • Figure 2 illustrates a sectional view of the plating cell and a head assembly during an immersion process.
  • Figure 3 illustrates a time diagram of an immersion process in connection with one or more embodiments of the invention.
  • Figure 4 illustrates a flow diagram of a method for immersing a substrate into a plating solution in accordance with one or more embodiments of the invention.
  • Figure 5 illustrates a total current supplied to a substrate in accordance with an embodiment of the invention as compared to prior art.
  • FIG. 1 illustrates an exemplary plating cell 100 that may be used in connection with one or more embodiments of the invention.
  • the plating cell 100 generally includes an outer basin 101 and an inner basin 102 positioned within the outer basin 101.
  • the inner basin 102 is generally configured to contain a plating solution that is used to plate a metal, e.g., copper, onto a substrate during an electrochemical plating process.
  • the plating solution is generally continuously supplied to the inner basin 102, and therefore, the plating solution continually overflows the uppermost point (generally termed a "weir") of the inner basin 102 and is collected by the outer basin 101 and drained therefrom for chemical management and recirculation.
  • the plating cell 100 may be generally positioned at a tilt angle, i.e., a frame portion 103 of the plating cell 100 may generally be elevated on one side such that the components of the plating cell 100 are tilted between about 3° and about 30°, or generally between about 4° and about 10° for optimal results.
  • the frame member 103 of the plating cell 100 supports an annular base member 104 on an upper portion thereof. Since the frame member
  • base member 104 is elevated on one side, the upper surface of base member 104, generally planar, is generally tilted from the horizontal at an angle that corresponds to the tilt angle of the frame member 103 relative to a horizontal position.
  • the base member 104 includes an annular or disk shaped recess formed into a central portion thereof, the annular recess being configured to receive a disk shaped anode member 105.
  • the base member 104 further includes a plurality of fluid inlets/drains 109 extending from a lower surface thereof. Each of the fluid inlets/drains 109 are generally configured to individually supply or drain a fluid to or from either the anode compartment or the cathode compartment of plating cell 100.
  • the 105 generally includes a plurality of slots 107 formed therethrough, wherein the slots 107 are generally positioned in parallel orientation with each other across the surface of the anode member 105.
  • the parallel orientation allows for dense fluids generated at the anode surface to flow downwardly across the anode surface and into one of the slots 107.
  • the plating cell 100 may further include a membrane support 106.
  • the membrane support 106 is generally secured at an outer periphery thereof to the base member 104, and includes an interior region configured to allow fluids to pass therethrough.
  • a membrane 108 which is generally an ionic membrane configured to selectively allow transmission of ions therethrough, is stretched across a lower surface of the membrane support 106 and operates to fluidly separate a catholyte chamber and anolyte chamber portions of the plating cell 100.
  • the membrane support 106 may include an o-ring type seal positioned near a perimeter of the membrane, wherein the seal is configured to prevent fluids from traveling from one side of the membrane 108 secured on the membrane support 106 to the other side of the membrane 108.
  • a diffusion plate 110 which is generally a porous ceramic disk member is configured to generate a substantially laminar flow or even flow of fluid in the direction of the substrate being plated, may optionally be positioned in the cell between the membrane 108 and the substrate being plated.
  • a more detailed description of the plating cell 100 may be found in commonly assigned United States Patent Application Serial No. 10/781 ,040, which was filed on February 18, 2004 under the title "METHOD FOR IMMERSING A SUBSTRATE”, claiming priority to United States Provisional Application Serial No. 60/448,575, which was filed on February 18, 2003, both of which are incorporated herein by reference in their entireties to the extent that these applications are not inconsistent with the present invention.
  • FIG. 2 illustrates an exemplary head assembly 200 used in connection with the plating cell 100.
  • the head assembly 200 may include a contact ring 202 and a thrust plate assembly 204.
  • a more detailed description of the contact ring 202 and thrust plate assembly 204 may be found in commonly assigned U.S. Patent Application Serial No. 10/278,527, which was filed on October 22, 2002 under the title "PLATING UNIFORMITY CONTROL BY CONTACT RING SHAPING", and commonly assigned United States Patent No. 6,251 ,236 entitled “CATHODE CONTACT RING FOR ELECTROCHEMICAL DEPOSITION,” both of which are hereby incorporated by reference in their entirety to the extent not inconsistent with the present invention.
  • the substrate may be secured to the contact ring 202, and the lower portion of the head assembly 200, i.e., the combination of the contact ring 202 and the thrust plate assembly 204, may be positioned at a tilt angle.
  • the lower portion of head assembly 200 and the plating surface of the substrate positioned on the contact ring 202 may be tilted to the tilt angle as a result of the movement of the head assembly 200.
  • the tilt angle is defined as the angle between horizontal and the plating surface/production surface of the substrate secured to the contact ring 202.
  • the tilt angle is generally between about 3° and about 30°, and more particularly, between about 3° and about 10°.
  • a pivot point 208 may be positioned such that when the head assembly is tilted, a central vertical axis of the substrate remains in substantially the same location as when the substrate was
  • the pivot point 208 may be positioned proximate the contact ring 202.
  • the head assembly 200 may be actuated in the Z-direction to begin the immersion process.
  • the lower side of the contact ring 202 contacts the plating solution as the head assembly 200 is actuated toward the plating cell 100.
  • the process of actuating the head assembly 200 toward the plating cell 100 may further include imparting rotational movement to the contact ring 202.
  • the contact ring 202 may be actuated in a vertical or Z-direction, while also being rotated about a central axis that intersects the radial center of the substrate, which is also generally orthogonal to the substrate surface.
  • the Z-motion of the head assembly 200 may be slowed and/or terminated and the tilt position of the contact ring 202 may be returned to horizontal.
  • This process generates a unique movement that includes both vertical actuation and tilt angle actuation, which has been shown to reduce bubble formation and adherence to the substrate surface during the immersion process.
  • the vertical and pivotal actuation of the substrate during immersion process may also include rotational movement of the contact ring 202, which has been shown to further minimize bubble formation and adherence to the substrate surface during the immersion process.
  • the head assembly 200 may further be actuated in a vertical direction (downward) and be pivoted about the pivot point 208, to further immerse the substrate into the plating solution.
  • the head assembly 200 may again be pivoted about the pivot point 208, so the substrate surface may be positioned in parallel relationship to the upper surface of the anode 105.
  • These various processes may also include rotating the substrate, which operates to dislodge any bubbles formed during the immersion process from the substrate surface.
  • Figure 3 illustrates a time diagram 300 of an immersion process in connection with one or more embodiments of the invention.
  • Stage 310 refers to a time period during which the substrate is immersed into the plating solution. The time period covered by stage 310 spans from when the substrate first contacts the plating solution to when the substrate is fully immersed. In one embodiment, stage 310 lasts from about 0.10 seconds to about 1.0 second.
  • Stage 320 refers to a time period from the moment the substrate is fully immersed to the moment the substrate is situated in a plating position, in one embodiment, stage 320 lasts from about 1 second to about 5 seconds.
  • Stage 330 refers to a time period during which the substrate is in a plating position. The plating position is defined as the position during which a conventional plating waveform is applied to completely fill the largest features on the substrate and overplate the substrate to a final total thickness.
  • FIG. 4 illustrates a flow diagram of a method 400 for immersing a substrate into a plating solution in accordance with one or more embodiments of the invention.
  • a first waveform is applied to the substrate as the substrate is immersed into the plating solution.
  • a waveform is a sequence of voltages or currents designed to control the current density on the substrate surface.
  • the waveform may comprise a constant voltage or current, a series of voltage or current steps, a gradually or periodically varying voltage or current, a pulsed voltage or current, or any combination of the above.
  • the voltage may be applied to the entire cell or to the substrate relative to a reference electrode 250 disposed inside the plating solution, as shown in Figure 2.
  • the waveforms discussed herein may be implemented in several ways. These ways include varying the voltage or current under recipe control, in response to a substrate position sensor, or in response to a direct measure of voltage or current passing through the cell. Recipe control is defined as applying a waveform in which the voltage or current are varied in time in a predetermined manner based on the expected trajectory of the substrate. As such, recipe control is distinct from schemes where the applied voltage or current vary in response to a sensor that actively detects the position, voltage, or current on the substrate in real time. Recipe control may be necessary for certain advanced processes where the time period
  • a typical implementation of recipe control involves performing a number of experiments or calculations to identify the desired duration for each voltage or current to be applied. Once known, these voltages and currents constitute a predetermined waveform that can be applied thereafter every time a substrate is processed.
  • step 410 occurs during stage 310.
  • the time period during which the first waveform is applied may last from the moment the substrate first contacts the plating solution to the moment the substrate is fully immersed. That time period may last from about 0.10 seconds to about 1.0 second.
  • the first waveform includes a constant voltage.
  • the first waveform may include a voltage such that the resulting current density on the substrate exceeds the threshold for pinch-off voids.
  • This threshold is a predetermined current density that would lead to the formation of pinch-off voids if maintained throughout stages 310 and 320.
  • the predetermined threshold required to create a pinch-off void is primarily a function of feature size; however, it may also be a function of plating solution chemistry and seed layer profile and thickness.
  • the first waveform comprises a voltage that is ramped, i.e., increases over time.
  • the first waveform comprises a sequence of voltages that increases over time.
  • the first waveform comprises a voltage that is stepped or muitistepped, i.e., includes two or more constant voltages, wherein each successive voltage is different from the previous voltage.
  • application of the first waveform is configured to ensure that the feature filling process occurs at all points on the substrate within a suitable current density window and to facilitate uniform deposition of metal ions across the substrate.
  • the first waveform has been described as being voltage controlled, other embodiments of the invention contemplate the first waveform as being current controlled.
  • applying the first waveform includes applying a first voltage to the substrate as the substrate first contacts the plating solution, stopping the application of the first constant voltage to the substrate after a predetermined period of time (or after a predetermined amount of current supplied to the substrate is reached), and supplying a first current to the substrate from the moment the predetermined period of time ends (or from the moment the predetermined amount of current is reached) to the moment the substrate is completely immersed.
  • the substrate first contacts the plating solution there is a short period of time during which the plating solution climbs up the substrate surface due to capillary forces, thereby creating a wicking effect.
  • the first constant voltage may be configured to take into account this wicking effect.
  • the first current is configured to take into account the fluid dynamics changes in vertical velocity, swing motion and rotation of the substrate and capillary forces of the plating solution.
  • the first constant voltage and the first current may each be a function of seed layer thickness, feature size, plating solution concentration, substrate size and plating cell geometry/design.
  • step 420 once the substrate is fully immersed, application of the first waveform is stopped and a second waveform is applied to the substrate from the time the substrate is fully immersed to the time the substrate is situated into a plating position.
  • step 420 occurs during stage 320.
  • the time period during which the second waveform is applied lasts from the moment the substrate is fully immersed to the moment the substrate is situated in a plating position.
  • the second waveform may be applied for about 1 second to about 5 seconds.
  • the first and second waveforms are applied to the substrate prior to the substrate being situated in the plating position.
  • the second waveform may also continue to be applied to the substrate for a predetermined period of time after the substrate is situated in the plating position (stage 330).
  • the second waveform includes a constant current.
  • the second waveform includes a current less than a predetermined threshold configured to perform a bottom-up fill.
  • the predetermined threshold required to initiate a bottom-up fill is typically a function of feature size, plating solution chemistry and seed layer thickness.
  • a bottom-up fill refers to a higher rate of deposition at the bottom of a feature than at the sidewalls.
  • application of the second waveform may be configured to grow and thicken a conformal metal layer on the seed layer prior to filling the features or prior to a bottom-up fill.
  • the second waveform includes a current that starts from below about a predetermined threshold configured to perform a bottom- up fill and increases as the thickness of a layer of deposit from the plating solution to the substrate increases.
  • application of the second waveform may be configured to ensure that the feature filling process occurs at all points on the substrate within a suitable current density window and to facilitate uniform deposition of metal ions across the substrate.
  • step 420 may include application of a pulsed voltage or current prior to the application of the various embodiments of second waveform described above.
  • the pulsed voltage or current may be greater than a predetermined threshold configured to create a pinch-off void inside a feature.
  • the pulsed voltage or current may be configured to enhance or attract metal ions contained inside the plating solution to portions of the substrate where the seed layer coverage is thin, patchy or completely absent.
  • a plating waveform is applied to the substrate (step 430).
  • the plating waveform is defined as a waveform designed to complete the filling of the largest features on the substrate and overplate the substrate to the desired final thickness of the deposit.
  • a plating waveform may consist of a sequence of one or more constant current steps.
  • application of the second waveform is stopped before the substrate is situated in the plating position and the plating waveform is applied to the substrate while the substrate is still being situated into the plating position.
  • the second waveform continues to be applied to the substrate for a predetermined period of time while the substrate is in the plating position before the plating waveform is applied.
  • stage 310 a first waveform having a constant cell voltage of 2 V, which corresponds to a current density of 5 mA/cm 2 on a fully immersed substrate, is applied for about 0.7 sec.
  • stage 320 a second waveform having a constant current equivalent to 3 mA/cm 2 is applied for about 1 to 4 seconds.
  • a typical plating waveform which is a sequence of three constant-current steps beginning at the end of stage 320.
  • An example of the plating waveform includes depositing 500 A at a current density of 5 mA/cm 2 , followed by depositing 1000 ⁇ at a current density of 10 mA/cm 2 , and followed by depositing 8500 A at a current density of 40 mA/cm 2 .
  • the above example applies to the case of a 300 mm wafer with a 500 A seed layer, trench features that are 55 nm wide and 150 nm deep, and via features that are 80 nm in diameter and 360 nm deep.
  • the plating bath used contained 40 g/L copper, 10 g/L acid, 50 ppm chloride, and optimized concentrations of plating additives such as the Enthone Viaform accelerator, suppressor, and leveler.
  • an example of the prior art may include applying a cell voltage of 2 V for the duration of stages 310 and 320, then applying a typical plating waveform from the end of stage 320.
  • An example of the invention in view of a prior art example is illustrated in Figure 5, which shows the total current supplied to the substrate as a result of the applied waveforms. While the prior art example is suitable for larger feature sizes, it often leads to significant pinch-off voids for the feature sizes mentioned above.

Abstract

A method for immersing a substrate into a plating solution. In one embodiment, the method includes applying a first waveform to the substrate as the substrate is being immersed into the plating solution, stopping the application of the first waveform to the substrate as soon as the substrate is fully immersed inside the plating solution, and applying a second waveform to the substrate prior to the substrate being situated into a plating position.

Description

generally contains a source of metal that is to be plated onto the surface of the substrate, and therefore, the application of the electrical bias causes the metal source to be plated onto the biased seed layer, thus depositing a layer of the ions on the substrate surface that fills the features.
[0004] However, one challenge associated with ECP processes is that the plating solutions, which are generally acidic, may chemically etch the seed layer during the process of immersing the substrate in the plating solution. Inasmuch as seed layers are generally relatively thin conductive layers, the chemical etching that may take place during the immersion process may result in conductive discontinuities in the seed layer, which may cause plating irregularities in the subsequent plating processes. Therefore, in order to prevent chemical etching during the immersion process, conventional electroplating systems apply an electrical loading bias to the substrate seed layer during the immersion process. The loading bias is generally configured to apply a cathodic bias to the substrate in order to prevent the chemical etching process and to cause at least some forward plating to occur. In a conventional process, the loading bias is a constant voltage applied to the substrate as the substrate is immersed in the plating solution and is maintained until the wafer reaches its plating position. The loading bias must be high enough to protect the seed layer from chemical etching and is in many cases higher for thinner seeds. In general, smaller features require thinner seeds. Therefore, as features become smaller, the required loading bias increases. It may also be desirable to further increase the loading bias beyond the level required to protect the seed layer in order to enhance nucleation of the electrodeposit.
[0005] However, for smaller features (e.g., about 65 nm or smaller), the conventional process is subject to failure for a number of problems. For example, the loading bias applied during the immersion may fill small features if it is sustained until the plating position is reached. However, this can lead to the formation of undesirable pinch-off voids. A pinch-off void is typically created when the current density on the sidewalls of a feature is high enough compared to the current density at the bottom of the feature such that the feature opening closes before the feature is fully filled. Further, in the early stages of the immersion process, i.e., when the
2 substrate first contacts the plating solution, very high current densities have been detected across the wet area of the substrate. These initially high current densities can introduce extremely undesirable effects, such as surface defects, gas bubbles and non-uniform conditions across the surface of the substrate. Further, as the surface of the substrate is immersed in the tilting motion under the constant load bias, the conductive area of the substrate being immersed is changing (increasing), and therefore, the resistance of the conductive path is also changing (decreasing). As a result of the changes in the current path during the immersion process, the current density applied across the surface of the substrate varies through the immersion process. Although the immersion process may only take a few seconds, the uniformity of the initial electrodeposit may be affected by the varying current density applied across the surface of the seed layer, and therefore, the uniformity of layers subsequently plated over the seed layer may also be affected.
[0006] Therefore, a need exists in the art for an improved method for controlling the current density on the substrate during immersion.
SUMMARY OF THE INVENTION
[0007] One or more embodiments of the present invention are generally directed to a method for immersing a substrate into a plating solution. The method includes applying a first waveform to the substrate as the substrate is being immersed into the plating solution, stopping the application of the first waveform to the substrate as soon as the substrate is fully immersed inside the plating solution, and applying a second waveform to the substrate prior to the substrate being situated into a plating position.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] So that the manner in which the above recited features of the present invention can be understood in detail, a more particular description of the invention, briefly summarized above, may be had by reference to embodiments, some of 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.
[0009] Figure 1 illustrates a plating cell that may be used in connection with one or more embodiments of the invention.
[0010] Figure 2 illustrates a sectional view of the plating cell and a head assembly during an immersion process.
[0011] Figure 3 illustrates a time diagram of an immersion process in connection with one or more embodiments of the invention.
[0012] Figure 4 illustrates a flow diagram of a method for immersing a substrate into a plating solution in accordance with one or more embodiments of the invention.
[0013] Figure 5 illustrates a total current supplied to a substrate in accordance with an embodiment of the invention as compared to prior art.
DETAILED DESCRIPTION
[0014] Figure 1 illustrates an exemplary plating cell 100 that may be used in connection with one or more embodiments of the invention. The plating cell 100 generally includes an outer basin 101 and an inner basin 102 positioned within the outer basin 101. The inner basin 102 is generally configured to contain a plating solution that is used to plate a metal, e.g., copper, onto a substrate during an electrochemical plating process. During the plating process, the plating solution is generally continuously supplied to the inner basin 102, and therefore, the plating solution continually overflows the uppermost point (generally termed a "weir") of the inner basin 102 and is collected by the outer basin 101 and drained therefrom for chemical management and recirculation. The plating cell 100 may be generally positioned at a tilt angle, i.e., a frame portion 103 of the plating cell 100 may generally be elevated on one side such that the components of the plating cell 100 are tilted between about 3° and about 30°, or generally between about 4° and about 10° for optimal results. The frame member 103 of the plating cell 100 supports an annular base member 104 on an upper portion thereof. Since the frame member
4 103 is elevated on one side, the upper surface of base member 104, generally planar, is generally tilted from the horizontal at an angle that corresponds to the tilt angle of the frame member 103 relative to a horizontal position. The base member
104 includes an annular or disk shaped recess formed into a central portion thereof, the annular recess being configured to receive a disk shaped anode member 105. The base member 104 further includes a plurality of fluid inlets/drains 109 extending from a lower surface thereof. Each of the fluid inlets/drains 109 are generally configured to individually supply or drain a fluid to or from either the anode compartment or the cathode compartment of plating cell 100. The anode member
105 generally includes a plurality of slots 107 formed therethrough, wherein the slots 107 are generally positioned in parallel orientation with each other across the surface of the anode member 105. The parallel orientation allows for dense fluids generated at the anode surface to flow downwardly across the anode surface and into one of the slots 107.
[0015] The plating cell 100 may further include a membrane support 106. The membrane support 106 is generally secured at an outer periphery thereof to the base member 104, and includes an interior region configured to allow fluids to pass therethrough. A membrane 108, which is generally an ionic membrane configured to selectively allow transmission of ions therethrough, is stretched across a lower surface of the membrane support 106 and operates to fluidly separate a catholyte chamber and anolyte chamber portions of the plating cell 100. The membrane support 106 may include an o-ring type seal positioned near a perimeter of the membrane, wherein the seal is configured to prevent fluids from traveling from one side of the membrane 108 secured on the membrane support 106 to the other side of the membrane 108. A diffusion plate 110, which is generally a porous ceramic disk member is configured to generate a substantially laminar flow or even flow of fluid in the direction of the substrate being plated, may optionally be positioned in the cell between the membrane 108 and the substrate being plated. A more detailed description of the plating cell 100 may be found in commonly assigned United States Patent Application Serial No. 10/781 ,040, which was filed on February 18, 2004 under the title "METHOD FOR IMMERSING A SUBSTRATE", claiming priority to United States Provisional Application Serial No. 60/448,575, which was filed on February 18, 2003, both of which are incorporated herein by reference in their entireties to the extent that these applications are not inconsistent with the present invention. Although one or more embodiments are described with referenced to a tilted plating cell, such as the plating cell 100, other embodiments may be implemented in other types of plating cells, such as one described in commonly assigned United States Patent Application Serial No. 10/135,546, which was filed on April 29, 2002 under the title "APPARATUS AND METHOD FOR REGULATING THE ELECTRICAL POWER APPLIED TO A SUBSTRATE DURING IMMERSION," which is incorporated herein by reference.
[0016] Figure 2 illustrates an exemplary head assembly 200 used in connection with the plating cell 100. The head assembly 200 may include a contact ring 202 and a thrust plate assembly 204. A more detailed description of the contact ring 202 and thrust plate assembly 204 may be found in commonly assigned U.S. Patent Application Serial No. 10/278,527, which was filed on October 22, 2002 under the title "PLATING UNIFORMITY CONTROL BY CONTACT RING SHAPING", and commonly assigned United States Patent No. 6,251 ,236 entitled "CATHODE CONTACT RING FOR ELECTROCHEMICAL DEPOSITION," both of which are hereby incorporated by reference in their entirety to the extent not inconsistent with the present invention.
[0017] The substrate may be secured to the contact ring 202, and the lower portion of the head assembly 200, i.e., the combination of the contact ring 202 and the thrust plate assembly 204, may be positioned at a tilt angle. The lower portion of head assembly 200 and the plating surface of the substrate positioned on the contact ring 202 may be tilted to the tilt angle as a result of the movement of the head assembly 200. The tilt angle is defined as the angle between horizontal and the plating surface/production surface of the substrate secured to the contact ring 202. The tilt angle is generally between about 3° and about 30°, and more particularly, between about 3° and about 10°. Further, a pivot point 208 may be positioned such that when the head assembly is tilted, a central vertical axis of the substrate remains in substantially the same location as when the substrate was
6 positioned horizontally, i.e., the pivot point 208 may be positioned proximate the contact ring 202.
[0018] Once the head assembly 200 is tilted, it may be actuated in the Z-direction to begin the immersion process. As the head assembly 200 is moved toward the plating cell 100, the lower side of the contact ring 202 contacts the plating solution as the head assembly 200 is actuated toward the plating cell 100. The process of actuating the head assembly 200 toward the plating cell 100 may further include imparting rotational movement to the contact ring 202. Thus, during the initial stages of the immersion process, the contact ring 202 may be actuated in a vertical or Z-direction, while also being rotated about a central axis that intersects the radial center of the substrate, which is also generally orthogonal to the substrate surface.
[0019] As the substrate becomes immersed in the plating solution contained within the plating cell 100, the Z-motion of the head assembly 200 may be slowed and/or terminated and the tilt position of the contact ring 202 may be returned to horizontal. This process generates a unique movement that includes both vertical actuation and tilt angle actuation, which has been shown to reduce bubble formation and adherence to the substrate surface during the immersion process. Further, the vertical and pivotal actuation of the substrate during immersion process may also include rotational movement of the contact ring 202, which has been shown to further minimize bubble formation and adherence to the substrate surface during the immersion process.
[0020] Once the substrate is completely immersed into the plating solution contained within the plating cell 100, the head assembly 200 may further be actuated in a vertical direction (downward) and be pivoted about the pivot point 208, to further immerse the substrate into the plating solution. Once the substrate is positioned deeper within the plating solution, the head assembly 200 may again be pivoted about the pivot point 208, so the substrate surface may be positioned in parallel relationship to the upper surface of the anode 105. These various processes may also include rotating the substrate, which operates to dislodge any bubbles formed during the immersion process from the substrate surface. [0021] Figure 3 illustrates a time diagram 300 of an immersion process in connection with one or more embodiments of the invention. Stage 310 refers to a time period during which the substrate is immersed into the plating solution. The time period covered by stage 310 spans from when the substrate first contacts the plating solution to when the substrate is fully immersed. In one embodiment, stage 310 lasts from about 0.10 seconds to about 1.0 second. Stage 320 refers to a time period from the moment the substrate is fully immersed to the moment the substrate is situated in a plating position, in one embodiment, stage 320 lasts from about 1 second to about 5 seconds. Stage 330 refers to a time period during which the substrate is in a plating position. The plating position is defined as the position during which a conventional plating waveform is applied to completely fill the largest features on the substrate and overplate the substrate to a final total thickness.
[0022] Figure 4 illustrates a flow diagram of a method 400 for immersing a substrate into a plating solution in accordance with one or more embodiments of the invention. At step 410, a first waveform is applied to the substrate as the substrate is immersed into the plating solution. A waveform is a sequence of voltages or currents designed to control the current density on the substrate surface. The waveform may comprise a constant voltage or current, a series of voltage or current steps, a gradually or periodically varying voltage or current, a pulsed voltage or current, or any combination of the above. When the waveform involves applying a voltage, the voltage may be applied to the entire cell or to the substrate relative to a reference electrode 250 disposed inside the plating solution, as shown in Figure 2. The waveforms discussed herein may be implemented in several ways. These ways include varying the voltage or current under recipe control, in response to a substrate position sensor, or in response to a direct measure of voltage or current passing through the cell. Recipe control is defined as applying a waveform in which the voltage or current are varied in time in a predetermined manner based on the expected trajectory of the substrate. As such, recipe control is distinct from schemes where the applied voltage or current vary in response to a sensor that actively detects the position, voltage, or current on the substrate in real time. Recipe control may be necessary for certain advanced processes where the time period
8 over which the voltage or current must be varied is so short such that there is insufficient time to send the sensor signal, communicate it to the control system such as a computer, and analyze it before applying the next voltage or current. A typical implementation of recipe control involves performing a number of experiments or calculations to identify the desired duration for each voltage or current to be applied. Once known, these voltages and currents constitute a predetermined waveform that can be applied thereafter every time a substrate is processed.
[0023] In view of Figure 3, step 410 occurs during stage 310. As such, the time period during which the first waveform is applied may last from the moment the substrate first contacts the plating solution to the moment the substrate is fully immersed. That time period may last from about 0.10 seconds to about 1.0 second. In one embodiment, the first waveform includes a constant voltage. Surprisingly, the first waveform may include a voltage such that the resulting current density on the substrate exceeds the threshold for pinch-off voids. This threshold is a predetermined current density that would lead to the formation of pinch-off voids if maintained throughout stages 310 and 320. The predetermined threshold required to create a pinch-off void is primarily a function of feature size; however, it may also be a function of plating solution chemistry and seed layer profile and thickness.
[0024] In yet another embodiment, the first waveform comprises a voltage that is ramped, i.e., increases over time. In still another embodiment, the first waveform comprises a sequence of voltages that increases over time. In still yet another embodiment, the first waveform comprises a voltage that is stepped or muitistepped, i.e., includes two or more constant voltages, wherein each successive voltage is different from the previous voltage. In such embodiments, application of the first waveform is configured to ensure that the feature filling process occurs at all points on the substrate within a suitable current density window and to facilitate uniform deposition of metal ions across the substrate. Although the first waveform has been described as being voltage controlled, other embodiments of the invention contemplate the first waveform as being current controlled. [0025] In yet another embodiment, applying the first waveform includes applying a first voltage to the substrate as the substrate first contacts the plating solution, stopping the application of the first constant voltage to the substrate after a predetermined period of time (or after a predetermined amount of current supplied to the substrate is reached), and supplying a first current to the substrate from the moment the predetermined period of time ends (or from the moment the predetermined amount of current is reached) to the moment the substrate is completely immersed. When the substrate first contacts the plating solution, there is a short period of time during which the plating solution climbs up the substrate surface due to capillary forces, thereby creating a wicking effect. This wicking effect may cause a high current density on the wet area of the substrate since the wet area is small and the cell resistance is low. Accordingly, the first constant voltage may be configured to take into account this wicking effect. As the substrate is being immersed into the plating solution, the fluid dynamics of the wet area of the substrate changes. As such, the first current is configured to take into account the fluid dynamics changes in vertical velocity, swing motion and rotation of the substrate and capillary forces of the plating solution. Further, the first constant voltage and the first current may each be a function of seed layer thickness, feature size, plating solution concentration, substrate size and plating cell geometry/design.
[0026] Referring now to step 420, once the substrate is fully immersed, application of the first waveform is stopped and a second waveform is applied to the substrate from the time the substrate is fully immersed to the time the substrate is situated into a plating position. In one embodiment, step 420 occurs during stage 320. As such, the time period during which the second waveform is applied lasts from the moment the substrate is fully immersed to the moment the substrate is situated in a plating position. The second waveform may be applied for about 1 second to about 5 seconds. In this manner, the first and second waveforms are applied to the substrate prior to the substrate being situated in the plating position. However, the second waveform may also continue to be applied to the substrate for a predetermined period of time after the substrate is situated in the plating position (stage 330).
10 [0027] In one embodiment, the second waveform includes a constant current. In another embodiment, the second waveform includes a current less than a predetermined threshold configured to perform a bottom-up fill. The predetermined threshold required to initiate a bottom-up fill is typically a function of feature size, plating solution chemistry and seed layer thickness. A bottom-up fill refers to a higher rate of deposition at the bottom of a feature than at the sidewalls. In such an embodiment, application of the second waveform may be configured to grow and thicken a conformal metal layer on the seed layer prior to filling the features or prior to a bottom-up fill.
[0028] In another embodiment, the second waveform includes a current that starts from below about a predetermined threshold configured to perform a bottom- up fill and increases as the thickness of a layer of deposit from the plating solution to the substrate increases. In such an embodiment, in addition to growing and thickening a conformal metal layer on the seed layer prior to filling the features or prior to a bottom-up fill, application of the second waveform may be configured to ensure that the feature filling process occurs at all points on the substrate within a suitable current density window and to facilitate uniform deposition of metal ions across the substrate.
[0029] In yet another embodiment, step 420 may include application of a pulsed voltage or current prior to the application of the various embodiments of second waveform described above. The pulsed voltage or current may be greater than a predetermined threshold configured to create a pinch-off void inside a feature. In such an embodiment, the pulsed voltage or current may be configured to enhance or attract metal ions contained inside the plating solution to portions of the substrate where the seed layer coverage is thin, patchy or completely absent.
[0030] Once the substrate is situated in the plating position, a plating waveform is applied to the substrate (step 430). The plating waveform is defined as a waveform designed to complete the filling of the largest features on the substrate and overplate the substrate to the desired final thickness of the deposit. For example, a plating waveform may consist of a sequence of one or more constant current steps.
11 in one embodiment, application of the second waveform is stopped before the substrate is situated in the plating position and the plating waveform is applied to the substrate while the substrate is still being situated into the plating position. In another embodiment, the second waveform continues to be applied to the substrate for a predetermined period of time while the substrate is in the plating position before the plating waveform is applied.
[0031] A specific example is described below to further illustrate the invention. During stage 310, a first waveform having a constant cell voltage of 2 V, which corresponds to a current density of 5 mA/cm2 on a fully immersed substrate, is applied for about 0.7 sec. During stage 320, a second waveform having a constant current equivalent to 3 mA/cm2 is applied for about 1 to 4 seconds. This is followed by a typical plating waveform which is a sequence of three constant-current steps beginning at the end of stage 320. An example of the plating waveform includes depositing 500 A at a current density of 5 mA/cm2, followed by depositing 1000 Λ at a current density of 10 mA/cm2, and followed by depositing 8500 A at a current density of 40 mA/cm2. The above example applies to the case of a 300 mm wafer with a 500 A seed layer, trench features that are 55 nm wide and 150 nm deep, and via features that are 80 nm in diameter and 360 nm deep. The plating bath used contained 40 g/L copper, 10 g/L acid, 50 ppm chloride, and optimized concentrations of plating additives such as the Enthone Viaform accelerator, suppressor, and leveler. For comparison, an example of the prior art may include applying a cell voltage of 2 V for the duration of stages 310 and 320, then applying a typical plating waveform from the end of stage 320. An example of the invention in view of a prior art example is illustrated in Figure 5, which shows the total current supplied to the substrate as a result of the applied waveforms. While the prior art example is suitable for larger feature sizes, it often leads to significant pinch-off voids for the feature sizes mentioned above.
[0032] While the foregoing is directed to embodiments of the present 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.
12

Claims

What Is Claimed Is:
1. A method for immersing a substrate into a plating solution, comprising: applying a first waveform to the substrate as the substrate is being immersed into the plating solution; stopping the application of the first waveform to the substrate as soon as the substrate is fully immersed inside the plating solution; and applying a second waveform to the substrate prior to the substrate being situated into a plating position.
2. The method of claim 1 , further comprising: stopping the application of the second waveform once the substrate is situated in the plating position; and applying a plating waveform to the substrate.
3. The method of claim 1 , wherein the first waveform comprises a constant voltage.
4. The method of claim 1 , wherein the first waveform comprises a voltage greater than a predetermined threshold for creating a pinch-off void inside a feature on the substrate.
5. The method of claim 1 , wherein the first waveform comprises a voltage that increases over time.
6. The method of claim 1 , wherein the first waveform comprises a sequence of voltages that increases over time.
7. The method of claim 1 , wherein the first waveform comprises a first constant voltage and a second constant voltage higher than the first constant voltage.
8. The method of claim 1 , wherein applying the first waveform comprises:
13 applying a first constant voltage to the substrate as the substrate first contacts the plating solution; stopping the application of the first constant voltage to the substrate after a predetermined period of time and prior to the substrate being fully immersed in the plating solution; and supplying a current to the substrate from the moment the predetermined period of time ends to the moment the substrate is completely immersed.
9. The method of claim 8, wherein the predetermined period of time is from about 0.10 seconds to about 1.0 second.
10. The method of claim 1 , wherein applying the first waveform comprises: applying a first constant voltage to the substrate as the substrate first contacts the plating solution; stopping the application of the first constant voltage to the substrate after a predetermined current supplied to the substrate is reached; and supplying a current to the substrate from the moment the predetermined current supplied to the substrate is reached to the moment the substrate is completely immersed.
11. The method of claim 1 , wherein the first waveform is applied to the substrate from about 0.10 seconds to about 1.0 second.
12. The method of claim 1 , wherein the second waveform comprises a constant current,
13. The method of claim 1 , wherein the second waveform comprises a current less than a predetermined threshold for performing a bottom-up fill.
14. The method of claim 4, wherein the second waveform comprises a current less than a predetermined threshold for performing a bottom-up fill.
14
15. The method of claim 1 , further comprising stopping the application of the second waveform before the substrate is situated in the plating position; and applying a plating waveform to the substrate while the substrate is still being situated into the plating position.
16. The method of claim 4, further comprising stopping the application of the second waveform before the substrate is situated in the plating position; and applying a plating waveform to the substrate while the substrate is still being situated into the plating position.
17. The method of claim 13, further comprising stopping the application of the second waveform before the substrate is situated in the plating position; and applying a plating waveform to the substrate while the substrate is still being situated into the plating position.
18. The method of claim 1 , wherein the second waveform comprises a current that starts from below a predetermined threshold for performing a bottom-up fill and increases as the thickness of a layer of deposit from the plating solution to the substrate increases.
19. The method of claim 4, wherein the second waveform comprises a current that starts from below a predetermined threshold for performing a bottom-up fill and increases as the thickness of a layer of deposit from the plating solution to the substrate increases.
20. The method of claim 18, further comprising stopping the application of the second waveform before the substrate is situated in the plating position; and applying a plating waveform to the substrate while the substrate is still being situated into the plating position.
21. The method of claim 1 , wherein the second waveform comprises a pulsed current or a pulsed voltage.
15
22. The method of claim 4, wherein the second waveform comprises a pulsed current or a pulsed voltage,
23. The method of claim 1 , wherein the first waveform and the second waveform are applied under recipe control.
24. The method of claim 1 , further comprising immersing the substrate at an angle.
16
PCT/US2006/003025 2005-02-07 2006-01-31 Immersion process for electroplating applications WO2006086169A2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US11/052,443 US20060175201A1 (en) 2005-02-07 2005-02-07 Immersion process for electroplating applications
US11/052,443 2005-02-07

Publications (2)

Publication Number Publication Date
WO2006086169A2 true WO2006086169A2 (en) 2006-08-17
WO2006086169A3 WO2006086169A3 (en) 2007-11-15

Family

ID=36778835

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2006/003025 WO2006086169A2 (en) 2005-02-07 2006-01-31 Immersion process for electroplating applications

Country Status (3)

Country Link
US (1) US20060175201A1 (en)
TW (1) TW200632146A (en)
WO (1) WO2006086169A2 (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060237319A1 (en) * 2005-04-22 2006-10-26 Akira Furuya Planting process and manufacturing process for semiconductor device thereby, and plating apparatus
US20090114542A1 (en) * 2007-11-06 2009-05-07 Spansion Llc Process of forming an electronic device including depositing a conductive layer over a seed layer
EP2072644A1 (en) * 2007-12-21 2009-06-24 ETH Zürich, ETH Transfer Device and method for the electrochemical deposition of chemical compounds and alloys with controlled composition and or stoichiometry
WO2012174732A1 (en) * 2011-06-24 2012-12-27 Acm Research (Shanghai) Inc. Methods and apparatus for uniformly metallization on substrates
US10508358B2 (en) * 2012-09-17 2019-12-17 Government Of The United States Of America, As Represented By The Secretary Of Commerce Process for forming a transition zone terminated superconformal filling
US11579344B2 (en) 2012-09-17 2023-02-14 Government Of The United States Of America, As Represented By The Secretary Of Commerce Metallic grating
US20160102416A1 (en) * 2013-01-29 2016-04-14 Novellus Systems, Inc. Low copper/high halide electroplating solutions for fill and defect control
US11814743B2 (en) * 2020-06-15 2023-11-14 Taiwan Semiconductor Manufacturing Company, Ltd. Plating membrane

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6808612B2 (en) * 2000-05-23 2004-10-26 Applied Materials, Inc. Method and apparatus to overcome anomalies in copper seed layers and to tune for feature size and aspect ratio

Family Cites Families (96)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL170871B (en) * 1952-07-05 Nippon Electric Co PROCEDURE FOR THE REMOVAL OF HEAVY AND / OR TOXIC METALS FROM WASTE GAS.
US2882209A (en) * 1957-05-20 1959-04-14 Udylite Res Corp Electrodeposition of copper from an acid bath
US3649509A (en) * 1969-07-08 1972-03-14 Buckbee Mears Co Electrodeposition systems
US3727620A (en) * 1970-03-18 1973-04-17 Fluoroware Of California Inc Rinsing and drying device
US4027686A (en) * 1973-01-02 1977-06-07 Texas Instruments Incorporated Method and apparatus for cleaning the surface of a semiconductor slice with a liquid spray of de-ionized water
JPS5271871A (en) * 1975-12-11 1977-06-15 Nec Corp Washing apparatus
CH629542A5 (en) * 1976-09-01 1982-04-30 Inoue Japax Res METHOD AND DEVICE FOR GALVANIC MATERIAL DEPOSITION.
US4326940A (en) * 1979-05-21 1982-04-27 Rohco Incorporated Automatic analyzer and control system for electroplating baths
US4315059A (en) * 1980-07-18 1982-02-09 The United States Of America As Represented By The United States Department Of Energy Molten salt lithium cells
US4336114A (en) * 1981-03-26 1982-06-22 Hooker Chemicals & Plastics Corp. Electrodeposition of bright copper
US4376685A (en) * 1981-06-24 1983-03-15 M&T Chemicals Inc. Acid copper electroplating baths containing brightening and leveling additives
EP0076569B1 (en) * 1981-10-01 1986-08-27 EMI Limited Electroplating arrangements
US4428815A (en) * 1983-04-28 1984-01-31 Western Electric Co., Inc. Vacuum-type article holder and methods of supportively retaining articles
JPS6063987A (en) * 1983-09-17 1985-04-12 沖電気工業株式会社 Method of producing printed circuit board
US4510176A (en) * 1983-09-26 1985-04-09 At&T Bell Laboratories Removal of coating from periphery of a semiconductor wafer
US4518678A (en) * 1983-12-16 1985-05-21 Advanced Micro Devices, Inc. Selective removal of coating material on a coated substrate
US4519846A (en) * 1984-03-08 1985-05-28 Seiichiro Aigo Process for washing and drying a semiconductor element
DE3688840T2 (en) * 1985-12-24 1993-11-25 Gould Inc METHOD AND DEVICE FOR ELECTROPLATING A COPPER BLADE.
US4732785A (en) * 1986-09-26 1988-03-22 Motorola, Inc. Edge bead removal process for spin on films
US4891106A (en) * 1987-08-18 1990-01-02 Hughes Aircraft Company Method of forming nonmagnetic silver electrodes on quartz glass
US5230743A (en) * 1988-05-25 1993-07-27 Semitool, Inc. Method for single wafer processing in which a semiconductor wafer is contacted with a fluid
US5235995A (en) * 1989-03-27 1993-08-17 Semitool, Inc. Semiconductor processor apparatus with dynamic wafer vapor treatment and particulate volatilization
US5224504A (en) * 1988-05-25 1993-07-06 Semitool, Inc. Single wafer processor
US5092975A (en) * 1988-06-14 1992-03-03 Yamaha Corporation Metal plating apparatus
US5316974A (en) * 1988-12-19 1994-05-31 Texas Instruments Incorporated Integrated circuit copper metallization process using a lift-off seed layer and a thick-plated conductor layer
EP0422760A1 (en) * 1989-10-12 1991-04-17 Mitsubishi Rayon Co., Ltd Amorphous alloy and process for preparation thereof
US5287237A (en) * 1990-03-16 1994-02-15 Hitachi, Ltd. Antiferromagnetic film superior in corrosion resistance, magnetoresistance-effect element and magnetoresistance-effect head including such thin film
US5178813A (en) * 1990-03-23 1993-01-12 Kureha Kagaku Kogyo K.K. Method of producing poly(phenylene sulfide) fibers
US5222310A (en) * 1990-05-18 1993-06-29 Semitool, Inc. Single wafer processor with a frame
US5368711A (en) * 1990-08-01 1994-11-29 Poris; Jaime Selective metal electrodeposition process and apparatus
JP2524436B2 (en) * 1990-09-18 1996-08-14 インターナショナル・ビジネス・マシーンズ・コーポレイション Surface treatment method
DE69231971T2 (en) * 1991-01-24 2002-04-04 Wako Pure Chem Ind Ltd Solutions for surface treatment of semiconductors
JP2525521B2 (en) * 1991-06-25 1996-08-21 日本リーロナール株式会社 Electroless tin-lead alloy plating bath
JPH05211384A (en) * 1991-11-20 1993-08-20 Nec Corp Plating method of printed wiring board
US5486264A (en) * 1992-03-25 1996-01-23 The Trustees Of Columbia University Laser etching of semiconductors
JP3200468B2 (en) * 1992-05-21 2001-08-20 日本エレクトロプレイテイング・エンジニヤース株式会社 Wafer plating equipment
WO1994006953A1 (en) * 1992-09-15 1994-03-31 Atr Wire & Cable Co., Inc. Method and apparatus for electrolytically plating copper
US5643803A (en) * 1992-09-18 1997-07-01 Nippondenso Co., Ltd. Production method of a semiconductor dynamic sensor
US5482680A (en) * 1992-10-09 1996-01-09 Ballard Power Systems, Inc. Electrochemical fuel cell assembly with integral selective oxidizer
US5328589A (en) * 1992-12-23 1994-07-12 Enthone-Omi, Inc. Functional fluid additives for acid copper electroplating baths
US5384640A (en) * 1993-01-19 1995-01-24 Gaztech International Corporation Gas sample chamber for use with a source of coherent radiation
US5608943A (en) * 1993-08-23 1997-03-11 Tokyo Electron Limited Apparatus for removing process liquid
US5705050A (en) * 1996-04-29 1998-01-06 Sampson; Richard L. Electrolytic process and apparatus for the controlled oxidation and reduction of inorganic and organic species in aqueous solutions
US5415890A (en) * 1994-01-03 1995-05-16 Eaton Corporation Modular apparatus and method for surface treatment of parts with liquid baths
US5625170A (en) * 1994-01-18 1997-04-29 Nanometrics Incorporated Precision weighing to monitor the thickness and uniformity of deposited or etched thin film
US5885469B1 (en) * 1996-11-05 2000-08-08 Applied Materials Inc Topographical structure of an electrostatic chuck and method of fabricating same
US5528118A (en) * 1994-04-01 1996-06-18 Nikon Precision, Inc. Guideless stage with isolated reaction stage
IL109240A (en) * 1994-04-07 1998-02-22 Yeda Res & Dev Ion exchange membranes
US5651865A (en) * 1994-06-17 1997-07-29 Eni Preferential sputtering of insulators from conductive targets
US5705223A (en) * 1994-07-26 1998-01-06 International Business Machine Corp. Method and apparatus for coating a semiconductor wafer
US5516412A (en) * 1995-05-16 1996-05-14 International Business Machines Corporation Vertical paddle plating cell
US5643456A (en) * 1995-05-30 1997-07-01 The Regents Of The University Of California Process for the displacement of cyanide ions from metal-cyanide complexes
US5516418A (en) * 1995-06-26 1996-05-14 International Business Machines Corporation Patterned electroplating
US5597460A (en) * 1995-11-13 1997-01-28 Reynolds Tech Fabricators, Inc. Plating cell having laminar flow sparger
US5785833A (en) * 1996-04-29 1998-07-28 Vaughan; Daniel J. Process for removing iron from tin-plating electrolytes
US6203582B1 (en) * 1996-07-15 2001-03-20 Semitool, Inc. Modular semiconductor workpiece processing tool
US5883762A (en) * 1997-03-13 1999-03-16 Calhoun; Robert B. Electroplating apparatus and process for reducing oxidation of oxidizable plating anions and cations
US6174425B1 (en) * 1997-05-14 2001-01-16 Motorola, Inc. Process for depositing a layer of material over a substrate
JPH1180989A (en) * 1997-09-02 1999-03-26 Oki Electric Ind Co Ltd Plating apparatus
US6024856A (en) * 1997-10-10 2000-02-15 Enthone-Omi, Inc. Copper metallization of silicon wafers using insoluble anodes
US5882498A (en) * 1997-10-16 1999-03-16 Advanced Micro Devices, Inc. Method for reducing oxidation of electroplating chamber contacts and improving uniform electroplating of a substrate
US6391166B1 (en) * 1998-02-12 2002-05-21 Acm Research, Inc. Plating apparatus and method
US6423642B1 (en) * 1998-03-13 2002-07-23 Semitool, Inc. Reactor for processing a semiconductor wafer
US6565729B2 (en) * 1998-03-20 2003-05-20 Semitool, Inc. Method for electrochemically depositing metal on a semiconductor workpiece
US6197181B1 (en) * 1998-03-20 2001-03-06 Semitool, Inc. Apparatus and method for electrolytically depositing a metal on a microelectronic workpiece
US6113771A (en) * 1998-04-21 2000-09-05 Applied Materials, Inc. Electro deposition chemistry
WO1999054527A2 (en) * 1998-04-21 1999-10-28 Applied Materials, Inc. Electro-chemical deposition system and method of electroplating on substrates
US6071388A (en) * 1998-05-29 2000-06-06 International Business Machines Corporation Electroplating workpiece fixture having liquid gap spacer
US6080291A (en) * 1998-07-10 2000-06-27 Semitool, Inc. Apparatus for electrochemically processing a workpiece including an electrical contact assembly having a seal member
US6074544A (en) * 1998-07-22 2000-06-13 Novellus Systems, Inc. Method of electroplating semiconductor wafer using variable currents and mass transfer to obtain uniform plated layer
US6210555B1 (en) * 1999-01-29 2001-04-03 Faraday Technology Marketing Group, Llc Electrodeposition of metals in small recesses for manufacture of high density interconnects using reverse pulse plating
US6203684B1 (en) * 1998-10-14 2001-03-20 Faraday Technology Marketing Group, Llc Pulse reverse electrodeposition for metallization and planarization of a semiconductor substrates
US6251236B1 (en) * 1998-11-30 2001-06-26 Applied Materials, Inc. Cathode contact ring for electrochemical deposition
US6258220B1 (en) * 1998-11-30 2001-07-10 Applied Materials, Inc. Electro-chemical deposition system
US6613214B2 (en) * 1998-11-30 2003-09-02 Applied Materials, Inc. Electric contact element for electrochemical deposition system and method
US6267853B1 (en) * 1999-07-09 2001-07-31 Applied Materials, Inc. Electro-chemical deposition system
US6254760B1 (en) * 1999-03-05 2001-07-03 Applied Materials, Inc. Electro-chemical deposition system and method
US6340633B1 (en) * 1999-03-26 2002-01-22 Advanced Micro Devices, Inc. Method for ramped current density plating of semiconductor vias and trenches
US6585876B2 (en) * 1999-04-08 2003-07-01 Applied Materials Inc. Flow diffuser to be used in electro-chemical plating system and method
US6551484B2 (en) * 1999-04-08 2003-04-22 Applied Materials, Inc. Reverse voltage bias for electro-chemical plating system and method
US6557237B1 (en) * 1999-04-08 2003-05-06 Applied Materials, Inc. Removable modular cell for electro-chemical plating and method
US6551488B1 (en) * 1999-04-08 2003-04-22 Applied Materials, Inc. Segmenting of processing system into wet and dry areas
US6571657B1 (en) * 1999-04-08 2003-06-03 Applied Materials Inc. Multiple blade robot adjustment apparatus and associated method
US6582578B1 (en) * 1999-04-08 2003-06-24 Applied Materials, Inc. Method and associated apparatus for tilting a substrate upon entry for metal deposition
US6261733B1 (en) * 1999-05-10 2001-07-17 Agfa-Gevaert Silver salt diffusion transfer material sensitized for blue light
JP3835058B2 (en) * 1999-05-12 2006-10-18 スズキ株式会社 Outboard motor electrical component mounting structure
SG80035A1 (en) * 1999-05-27 2001-04-17 Inst Of Microelectronics Viterbi decoding of punctured convolutional codes without real-time branch metric computation
US6224737B1 (en) * 1999-08-19 2001-05-01 Taiwan Semiconductor Manufacturing Company Method for improvement of gap filling capability of electrochemical deposition of copper
US6399479B1 (en) * 1999-08-30 2002-06-04 Applied Materials, Inc. Processes to improve electroplating fill
US6395101B1 (en) * 1999-10-08 2002-05-28 Semitool, Inc. Single semiconductor wafer processor
US6423636B1 (en) * 1999-11-19 2002-07-23 Applied Materials, Inc. Process sequence for improved seed layer productivity and achieving 3mm edge exclusion for a copper metalization process on semiconductor wafer
US6409903B1 (en) * 1999-12-21 2002-06-25 International Business Machines Corporation Multi-step potentiostatic/galvanostatic plating control
US6562204B1 (en) * 2000-02-29 2003-05-13 Novellus Systems, Inc. Apparatus for potential controlled electroplating of fine patterns on semiconductor wafers
SE516623C2 (en) * 2000-06-15 2002-02-05 Electrolux Ab Safety device in the case of a washing machine door
EP1297727B1 (en) * 2000-06-20 2005-10-05 Koninklijke Philips Electronics N.V. Circuit device
US6551487B1 (en) * 2001-05-31 2003-04-22 Novellus Systems, Inc. Methods and apparatus for controlled-angle wafer immersion

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6808612B2 (en) * 2000-05-23 2004-10-26 Applied Materials, Inc. Method and apparatus to overcome anomalies in copper seed layers and to tune for feature size and aspect ratio

Also Published As

Publication number Publication date
WO2006086169A3 (en) 2007-11-15
TW200632146A (en) 2006-09-16
US20060175201A1 (en) 2006-08-10

Similar Documents

Publication Publication Date Title
WO2006086169A2 (en) Immersion process for electroplating applications
US6884335B2 (en) Electroplating using DC current interruption and variable rotation rate
US7854828B2 (en) Method and apparatus for electroplating including remotely positioned second cathode
TWI472650B (en) Pulse sequence for plating on thin seed layers
KR101765346B1 (en) Method and apparatus for electroplating
US9376758B2 (en) Electroplating method
US20060237325A1 (en) Cu ecp planarization by insertion of polymer treatment step between gap fill and bulk fill steps
US20100163408A1 (en) Plating apparatus and plating method
KR102297508B1 (en) Tsv bath evaluation using field versus feature contrast
KR20110127617A (en) Through silicon via filling using an electrolyte with a dual state inhibitor
KR102358030B1 (en) Method for uniform flow behavior in an electroplating cell
KR102550311B1 (en) Monitoring electrolytes during electroplating
US20150203983A1 (en) Plating method and plating apparatus
US20050218000A1 (en) Conditioning of contact leads for metal plating systems
WO2019079193A1 (en) Convection optimization for mixed feature electroplating
JP2002115097A (en) Method for impressing electrical biasing for enhancing metal deposition
US7285195B2 (en) Electric field reducing thrust plate
WO2014149245A1 (en) Electrochemical deposition processes for semiconductor wafers
US20040016648A1 (en) Tilted electrochemical plating cell with constant wafer immersion angle
US8277619B2 (en) Apparatus for electrochemical plating semiconductor wafers
US20040206628A1 (en) Electrical bias during wafer exit from electrolyte bath
KR20010015297A (en) Electrochemical deposition for high aspect ratio structures using electrical pulse modulation
US20060124468A1 (en) Contact plating apparatus
US20040192066A1 (en) Method for immersing a substrate
KR102208202B1 (en) Current ramping and current pulsing entry of substrates for electroplating

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application
NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 06719744

Country of ref document: EP

Kind code of ref document: A2