US20150068911A1 - Copper plating apparatus, copper plating method and method for manufacturing semiconductor device - Google Patents
Copper plating apparatus, copper plating method and method for manufacturing semiconductor device Download PDFInfo
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- US20150068911A1 US20150068911A1 US14/098,794 US201314098794A US2015068911A1 US 20150068911 A1 US20150068911 A1 US 20150068911A1 US 201314098794 A US201314098794 A US 201314098794A US 2015068911 A1 US2015068911 A1 US 2015068911A1
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- plating
- copper
- additive agent
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/38—Electroplating: Baths therefor from solutions of copper
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/002—Cell separation, e.g. membranes, diaphragms
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/12—Process control or regulation
- C25D21/14—Controlled addition of electrolyte components
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
- C25D17/001—Apparatus specially adapted for electrolytic coating of wafers, e.g. semiconductors or solar cells
Definitions
- Embodiments described herein relate generally to a copper plating apparatus, a copper plating method and a method for manufacturing a semiconductor device.
- interconnects are formed by plating copper on a silicon substrate when manufacturing a semiconductor device. Due to the shrinking of semiconductor devices in recent years, it is also necessary to increase the precision of the copper plating. Further, it is necessary to reduce the processing cost of the copper plating.
- FIG. 1 is a drawing showing a copper plating apparatus according to an embodiment
- FIG. 4 is a graph showing the change over time of the dust count of a comparative example, where the horizontal axis is the plating processing time after placing a new copper member, and the vertical axis is the dust count.
- a copper plating apparatus includes a plating tank configured to have a copper member and a plating member being disposed in an interior of the plating tank, a blocking film configured to partition the interior of the plating tank into an anode chamber where the copper member is to be disposed and a cathode chamber where the plating member is to be disposed, the blocking film being configured to transmit copper ions and not transmit an additive agent, a supply unit configured to supply the additive agent to the anode chamber, and a power supply configured to apply a voltage between the copper member and the plating member.
- a copper plating method includes disposing a copper member in an anode chamber of a plating tank, supplying plating liquid including an additive agent to the anode chamber, disposing a first plating member in a cathode chamber partitioned from the anode chamber by a blocking film configured to transmit copper ions and not transmit the additive agent, and supplying the plating liquid including the additive agent to the cathode chamber.
- the method includes applying a voltage to cause the copper member to be positive and the first plating member to be negative to perform copper plating on the first plating member and form a black film at a surface of the copper member.
- the method includes replacing the first plating member with a second plating member after the black film is formed.
- the method includes applying a voltage to cause the copper member to be positive and the second plating member to be negative to perform copper plating on the second plating member while supplying the additive agent to the cathode chamber without supplying the additive agent to the anode chamber.
- FIG. 1 is a drawing showing a copper plating apparatus according to the embodiment.
- a plating cell 10 As shown in FIG. 1 , a plating cell 10 , a plating liquid supply unit 11 , an additive agent supply unit 12 , and a plating liquid recovery unit 13 are provided in the copper plating apparatus 1 according to the embodiment.
- multiple plating cells 10 are provided for one set of the plating liquid supply unit 11 , the additive agent supply unit 12 , and the plating liquid recovery unit 13 .
- the leveler includes, for example, various dielectrics.
- the plating liquid recovery unit 13 is a unit that recovers the used plating liquid 106 .
- a pump (not shown) and a filter (not shown) are provided in the plating liquid supply unit 11 ; and a pump (not shown) and a filter (not shown) are provided in the additive agent supply unit 12 .
- An external tank 20 is provided in the plating cell 10 ; and a plating tank 21 is provided inside the external tank 20 .
- a blocking film 22 is provided in the interior of the plating tank 21 .
- the interior of the plating tank 21 is partitioned into an anode chamber 23 and a cathode chamber 24 by the blocking film 22 ; the anode chamber 23 is positioned at the lower portion of the plating tank 21 interior; and the cathode chamber 24 is positioned at the upper portion of the plating tank 21 interior.
- the blocking film 22 is a film, e.g., a membrane, e.g., an ion exchange film, that transmits copper ions and does not transmit the polymer material that is the component of the additive agent 107 .
- a resistance film 25 is provided inside the cathode chamber 24 of the plating tank 21 .
- the resistance film 25 is made of an insulating material such as a resin, a ceramic, etc., is a plate in which many fine holes are formed, and is a film used to provide resistance to the flow of the copper ions.
- the plating thickness formed on the silicon wafer becomes uniform by interposing the resistance film 25 between the anode and the cathode. Stepped portions for holding the blocking film 22 and the resistance film 25 are formed at the inner side surface of the plating tank 21 . To this end, the inner diameter of the plating tank 21 decreases downward in stages.
- a power supply plate 26 is provided at the bottom portion of the plating tank 21 to hold a copper member 100 , which is used as the plating material, and to apply a potential to the copper member 100 .
- a holder 27 is provided above the plating tank 21 to hold a silicon wafer 102 , which is the plating member, cause the silicon wafer 102 to rotate, and apply a potential.
- a power supply 28 is provided outside the external tank 20 to apply a voltage between the power supply plate 26 and the holder 27 to cause the power supply plate 26 to be positive and cause the holder 27 to be negative.
- a bath 31 that holds the plating liquid, pumps 32 and 33 that cause the plating liquid to flow, and filters 34 and 35 that remove dust from the plating liquid are provided outside the external tank 20 .
- a conduit 41 is connected between the anode chamber 23 of the plating tank 21 and the pump 32 ; a conduit 42 is connected between the pump 32 and the filter 34 ; and a conduit 43 is connected between the filter 34 and the anode chamber 23 .
- a conduit 48 is connected between the plating liquid supply unit 11 and the anode chamber 23 .
- a valve 49 is provided partway through the conduit 48 .
- a conduit 57 is connected between the bath 31 and a portion of the conduit 48 that is more on the plating liquid supply unit 11 side than is the valve 49 .
- a valve 58 is provided partway through the conduit 57 .
- a conduit 51 is connected between the additive agent supply unit 12 and the bath 31 .
- a valve 52 is provided partway through the conduit 51 .
- a conduit 53 is connected between the additive agent supply unit 12 and the conduit 41 .
- a valve 54 is provided partway through the conduit 53 .
- a conduit 55 is connected between the anode chamber 23 and the bath 31 .
- a valve 56 is provided partway through the conduit 55 .
- a conduit 59 is interposed between the bath 31 and the plating liquid recovery unit 13 .
- a valve 60 is provided partway through the conduit 59 .
- the operation of the copper plating apparatus 1 i.e., a copper plating method according to the embodiment, will now be described.
- the copper plating method according to the embodiment is a portion of a method for manufacturing a semiconductor device.
- FIG. 2 is a flowchart showing the copper plating method according to the embodiment.
- FIG. 3A to FIG. 3D are drawings showing the copper plating method according to the embodiment.
- step S 3 the anode chamber 23 interior is filled with the plating liquid 106 (the VMS) that does not include the additive agent 107 .
- the pump (not shown) inside the plating liquid supply unit 11 is caused to operate; the valve 49 is opened; and the pump 32 is caused to operate.
- the plating liquid 106 (the VMS) is supplied from the plating liquid supply unit 11 to the interior of the anode chamber 23 via the conduit 48 ; and the plating liquid 106 circulates through the anode-side circulation water path 37 .
- the valve 49 is closed.
- the additive agent 107 is supplied to the conduit 41 by opening the valve 54 .
- the additive agent 107 flows into the anode-side circulation water path 37 , mixes with the plating liquid 106 , and is supplied to the interior of the anode chamber 23 .
- the concentration of the additive agent 107 in the plating liquid 106 is set to be, for example, not less than 1 ppm.
- the valve 54 is closed.
- the plating liquid 106 is circulated inside the cathode-side circulation water path 38 .
- the additive agent supply unit 12 to operate and by opening the valve 52 , the additive agent 107 is introduced to the interior of the bath 31 and is supplied to the interior of the cathode chamber 24 via the cathode-side circulation water path 38 . Therefore, at this stage as shown in FIG. 3A , a mixed liquid of the plating liquid 106 and the additive agent 107 is supplied to both the interior of the anode chamber 23 and the interior of the cathode chamber 24 .
- the plating liquid 106 and the additive agent 107 that are inside the anode chamber 23 and the plating liquid 106 and the additive agent 107 that are inside the cathode chamber 24 are circulated independently through the circulation water paths.
- the plating liquid 106 can move between the anode chamber 23 and the cathode chamber 24 via the blocking film 22 , the movement of the additive agent 107 is blocked by the blocking film 22 .
- the plating amount for the silicon wafer 101 it is favorable for the plating amount for the silicon wafer 101 to be not less than (S ⁇ 14) coulombs, where the surface area of the region where the surface of the copper member 100 contacts the plating liquid 106 is S (cm 2 ). Thereby, the black film 108 can be reliably formed.
- step S 7 of FIG. 2 the quality of the copper plating layer 110 formed on the silicon wafer 101 is inspected. Then, if the quality is defective, the flow returns to step S 6 ; and the plating processing of the dummy silicon wafer 101 is continued. On the other hand, if the quality is good, the flow proceeds to step S 8 to transition to the main plating processing.
- FIG. 4 is a graph showing the change over time of the dust count of the comparative example, where the horizontal axis is the plating processing time after placing a new copper member, and the vertical axis is the dust count.
- the plating processing was performed using a new copper member 100 by supplying the plating liquid 106 not including the additive agent 107 to the interior of the anode chamber 23 and by supplying the plating liquid 106 including the additive agent 107 to the interior of the cathode chamber 24 .
- the reason that the dust count decreased after increasing once is because the additive agent 107 entered the anode chamber 23 little by little via the blocking film 22 ; and thereby, the black film 108 was formed. Therefore, it also may be considered to perform the plating processing by utilizing this phenomenon and waiting until the dust count decreases. However, in such a case, it is necessary to continue the plating processing of the dummy until the black film 108 is formed by the additive agent 107 leaking into the anode chamber 23 and the formation of the foreign matter 112 decreases sufficiently; and the productivity of the plating processing decreases. In an example, dummy plating processing for several days is necessary until the black film 108 is formed by the additive agent 107 leaking via the blocking film 22 and the dust count decreases. Conversely, according to the embodiment described above, transition to the main plating processing is possible when the plating processing of the dummy is performed for several minutes.
- the black film 108 that has become too thick comes off, mixes into the plating liquid 106 , and causes defects such as embedding defects, etc.
- the consumption of the additive agent 107 is high; and the cost of the plating processing increases. Further, it is necessary to frequently replace the filters 34 and 35 because the dust increases; and this also causes the cost to increase.
- a copper plating apparatus a copper plating method, and a method for manufacturing the semiconductor device can be realized to perform inexpensive and high-precision copper plating.
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Abstract
A copper plating apparatus according to an embodiment includes a plating tank configured to have a copper member and a plating member being disposed in an interior of the plating tank, a blocking film configured to partition the interior of the plating tank into an anode chamber where the copper member is to be disposed and a cathode chamber where the plating member is to be disposed, the blocking film being configured to transmit copper ions and not transmit an additive agent, a supply unit configured to supply the additive agent to the anode chamber, and a power supply configured to apply a voltage between the copper member and the plating member.
Description
- This application is based upon and claims the benefit of priority from U.S. Provisional Patent Application 61/876,976, filed on Sep. 12, 2013; the entire contents of which are incorporated herein by reference.
- Embodiments described herein relate generally to a copper plating apparatus, a copper plating method and a method for manufacturing a semiconductor device.
- Conventionally, interconnects, etc., are formed by plating copper on a silicon substrate when manufacturing a semiconductor device. Due to the shrinking of semiconductor devices in recent years, it is also necessary to increase the precision of the copper plating. Further, it is necessary to reduce the processing cost of the copper plating.
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FIG. 1 is a drawing showing a copper plating apparatus according to an embodiment; -
FIG. 2 is a flowchart showing the copper plating method according to the embodiment; -
FIG. 3A toFIG. 3D are drawings showing the copper plating method according to the embodiment; and -
FIG. 4 is a graph showing the change over time of the dust count of a comparative example, where the horizontal axis is the plating processing time after placing a new copper member, and the vertical axis is the dust count. - A copper plating apparatus according to an embodiment includes a plating tank configured to have a copper member and a plating member being disposed in an interior of the plating tank, a blocking film configured to partition the interior of the plating tank into an anode chamber where the copper member is to be disposed and a cathode chamber where the plating member is to be disposed, the blocking film being configured to transmit copper ions and not transmit an additive agent, a supply unit configured to supply the additive agent to the anode chamber, and a power supply configured to apply a voltage between the copper member and the plating member.
- A copper plating method according to an embodiment includes disposing a copper member in an anode chamber of a plating tank, supplying plating liquid including an additive agent to the anode chamber, disposing a first plating member in a cathode chamber partitioned from the anode chamber by a blocking film configured to transmit copper ions and not transmit the additive agent, and supplying the plating liquid including the additive agent to the cathode chamber. The method includes applying a voltage to cause the copper member to be positive and the first plating member to be negative to perform copper plating on the first plating member and form a black film at a surface of the copper member. The method includes replacing the first plating member with a second plating member after the black film is formed. And the method includes applying a voltage to cause the copper member to be positive and the second plating member to be negative to perform copper plating on the second plating member while supplying the additive agent to the cathode chamber without supplying the additive agent to the anode chamber.
- An embodiment of the invention will now be described with reference to the drawings.
-
FIG. 1 is a drawing showing a copper plating apparatus according to the embodiment. - As shown in
FIG. 1 , aplating cell 10, a platingliquid supply unit 11, an additiveagent supply unit 12, and a platingliquid recovery unit 13 are provided in thecopper plating apparatus 1 according to the embodiment. In thecopper plating apparatus 1,multiple plating cells 10 are provided for one set of the platingliquid supply unit 11, the additiveagent supply unit 12, and the platingliquid recovery unit 13. - The plating
liquid supply unit 11 is a unit that supplies a plating liquid 106 (VMS: Vergin Make up Solution) not including an additive agent 107 (referring toFIG. 3A ) to the platingcell 10. The platingliquid 106 is, for example, an aqueous copper sulfate solution. The additiveagent supply unit 12 is a unit that supplies theadditive agent 107 to the platingliquid 106. Theadditive agent 107 includes, for example, an accelerator that promotes the plating, a suppressor that suppresses the plating, and a leveler that levels the plating layer. The accelerator includes, for example, SPS (bis 3-sulfopropyl disulfide disodium). The suppressor includes, for example, PEG (polyethylene glycol). The leveler includes, for example, various dielectrics. The platingliquid recovery unit 13 is a unit that recovers the used platingliquid 106. A pump (not shown) and a filter (not shown) are provided in the platingliquid supply unit 11; and a pump (not shown) and a filter (not shown) are provided in the additiveagent supply unit 12. - An
external tank 20 is provided in theplating cell 10; and aplating tank 21 is provided inside theexternal tank 20. A blockingfilm 22 is provided in the interior of theplating tank 21. The interior of theplating tank 21 is partitioned into ananode chamber 23 and acathode chamber 24 by the blockingfilm 22; theanode chamber 23 is positioned at the lower portion of theplating tank 21 interior; and thecathode chamber 24 is positioned at the upper portion of theplating tank 21 interior. The blockingfilm 22 is a film, e.g., a membrane, e.g., an ion exchange film, that transmits copper ions and does not transmit the polymer material that is the component of theadditive agent 107. - A
resistance film 25 is provided inside thecathode chamber 24 of theplating tank 21. Theresistance film 25 is made of an insulating material such as a resin, a ceramic, etc., is a plate in which many fine holes are formed, and is a film used to provide resistance to the flow of the copper ions. The plating thickness formed on the silicon wafer becomes uniform by interposing theresistance film 25 between the anode and the cathode. Stepped portions for holding the blockingfilm 22 and theresistance film 25 are formed at the inner side surface of theplating tank 21. To this end, the inner diameter of theplating tank 21 decreases downward in stages. - Also, a
power supply plate 26 is provided at the bottom portion of theplating tank 21 to hold acopper member 100, which is used as the plating material, and to apply a potential to thecopper member 100. Above theplating tank 21, aholder 27 is provided to hold asilicon wafer 102, which is the plating member, cause thesilicon wafer 102 to rotate, and apply a potential. Apower supply 28 is provided outside theexternal tank 20 to apply a voltage between thepower supply plate 26 and theholder 27 to cause thepower supply plate 26 to be positive and cause theholder 27 to be negative. - In the plating
cell 10, abath 31 that holds the plating liquid,pumps external tank 20. - Further, a
conduit 41 is connected between theanode chamber 23 of theplating tank 21 and thepump 32; aconduit 42 is connected between thepump 32 and thefilter 34; and aconduit 43 is connected between thefilter 34 and theanode chamber 23. Thereby, an anode-sidecirculation water path 37 in which the platingliquid 106 circulates in the order of (anode chamber 23-conduit 41-pump 32-conduit 42-filter 34-conduit 43-anode chamber 23) is made. - Also, a
conduit 44 is connected between the bottom portion of theexternal tank 20 and thebath 31; aconduit 45 is connected between thebath 31 and thepump 33; aconduit 46 is connected between thepump 33 and thefilter 35; and aconduit 47 is connected between thefilter 35 and thecathode chamber 24 of theplating tank 21. Thereby, a cathode-sidecirculation water path 38 in which the platingliquid 106 circulates in the order of (cathode chamber 24-external tank 20-conduit 44-bath 31-conduit 45-pump 33-conduit 46-filter 35-conduit 47-cathode chamber 24) is made. - On the other hand, a
conduit 48 is connected between the platingliquid supply unit 11 and theanode chamber 23. Avalve 49 is provided partway through theconduit 48. Aconduit 57 is connected between thebath 31 and a portion of theconduit 48 that is more on the platingliquid supply unit 11 side than is thevalve 49. Avalve 58 is provided partway through theconduit 57. Aconduit 51 is connected between the additiveagent supply unit 12 and thebath 31. Avalve 52 is provided partway through theconduit 51. Aconduit 53 is connected between the additiveagent supply unit 12 and theconduit 41. Avalve 54 is provided partway through theconduit 53. Thereby, the additiveagent supply unit 12 can supply theadditive agent 107 to the anode-sidecirculation water path 37 via theconduit 53 and thevalve 54. - A
conduit 55 is connected between theanode chamber 23 and thebath 31. Avalve 56 is provided partway through theconduit 55. Aconduit 59 is interposed between thebath 31 and the platingliquid recovery unit 13. Avalve 60 is provided partway through theconduit 59. - The operation of the
copper plating apparatus 1, i.e., a copper plating method according to the embodiment, will now be described. The copper plating method according to the embodiment is a portion of a method for manufacturing a semiconductor device. -
FIG. 2 is a flowchart showing the copper plating method according to the embodiment. -
FIG. 3A toFIG. 3D are drawings showing the copper plating method according to the embodiment. - In
FIG. 3A toFIG. 3D , theadditive agent 107 is schematically illustrated by the gray circles. - First, as shown in
FIG. 1 , thecopper plating apparatus 1 is prepared. In thecopper plating apparatus 1 at this stage, the blockingfilm 22 and theresistance film 25 are not mounted inside theplating tank 21; thecopper member 100 and thesilicon wafer 102 are not mounted as well; and theplating liquid 106 is not introduced. Further, all of the valves are closed. - Then, as shown in step S1 of
FIG. 2 , anew copper member 100 is prepared; and the surface of thecopper member 100 is cleaned. For example, the surface of thecopper member 100 is etched using sulfuric acid or aqueous hydrogen peroxide; and subsequently, water rinse is performed. - Continuing as shown in step S2, the
copper member 100 is placed inside theanode chamber 23 of theplating tank 21 and connected to thepower supply plate 26. - Then, as shown in step S3, the
anode chamber 23 interior is filled with the plating liquid 106 (the VMS) that does not include theadditive agent 107. Specifically, the pump (not shown) inside the platingliquid supply unit 11 is caused to operate; thevalve 49 is opened; and thepump 32 is caused to operate. Thereby, the plating liquid 106 (the VMS) is supplied from the platingliquid supply unit 11 to the interior of theanode chamber 23 via theconduit 48; and theplating liquid 106 circulates through the anode-sidecirculation water path 37. When theanode chamber 23 is filled with theplating liquid 106, thevalve 49 is closed. - Continuing as shown in step S4, the
additive agent 107 is supplied to theconduit 41 by opening thevalve 54. Thereby, theadditive agent 107 flows into the anode-sidecirculation water path 37, mixes with theplating liquid 106, and is supplied to the interior of theanode chamber 23. At this time, the concentration of theadditive agent 107 in theplating liquid 106 is set to be, for example, not less than 1 ppm. Subsequently, thevalve 54 is closed. - Then, as shown in step S5 of
FIG. 2 andFIG. 3A , the platingcell 10 is assembled. Specifically, the blockingfilm 22 is mounted inside theplating tank 21; and theresistance film 25 is mounted. Then, adummy silicon wafer 101 is mounted to theholder 27. Then, theplating liquid 106 is supplied to the interior of theanode chamber 23 by opening thevalve 49. The plating liquid 106 that is supplied to the interior of theanode chamber 23 passes through the blockingfilm 22, enters thecathode chamber 24 as well, and fills theentire plating tank 21. - Continuing, the
plating liquid 106 and theadditive agent 107 that overflow from theplating tank 21 accumulate at the bottom portion of theexternal tank 20 and are returned to thebath 31 via theconduit 44. Also, by opening thevalve 60, a portion of theplating liquid 106 and theadditive agent 107 can be recovered into the platingliquid recovery unit 13 via theconduit 59. Thereby,new plating liquid 106 is constantly supplied to the interior of the platingcell 10. - Further, by causing the
pump 33 to operate, theplating liquid 106 is circulated inside the cathode-sidecirculation water path 38. Then, by causing the additiveagent supply unit 12 to operate and by opening thevalve 52, theadditive agent 107 is introduced to the interior of thebath 31 and is supplied to the interior of thecathode chamber 24 via the cathode-sidecirculation water path 38. Therefore, at this stage as shown inFIG. 3A , a mixed liquid of theplating liquid 106 and theadditive agent 107 is supplied to both the interior of theanode chamber 23 and the interior of thecathode chamber 24. However, theplating liquid 106 and theadditive agent 107 that are inside theanode chamber 23 and theplating liquid 106 and theadditive agent 107 that are inside thecathode chamber 24 are circulated independently through the circulation water paths. Although theplating liquid 106 can move between theanode chamber 23 and thecathode chamber 24 via the blockingfilm 22, the movement of theadditive agent 107 is blocked by the blockingfilm 22. - Then, as shown in step S6 of
FIG. 2 andFIG. 3B , a voltage is applied by thepower supply 28 to cause thecopper member 100 to be positive and thesilicon wafer 101 to be negative. Thereby, acopper plating layer 110 is formed by copper plating being performed on the surface of thedummy silicon wafer 101. At this time, monovalent copper ions (Cu+) and bivalent copper ions (Cu2+) are produced from thecopper member 100 and reach thesilicon wafer 101 by moving through theplating liquid 106. Then, the ions bond with electrons at the surface of thesilicon wafer 101 and precipitate as simple copper. - At this time,
foreign matter 112 forms at thecopper plating layer 110 due to the monovalent copper ions (Cu+). The formation of theforeign matter 112 reduces the uniformity of thecopper plating layer 110 and mixes into the plating liquid 106 to become dust. On the other hand, inside theanode chamber 23, ablack film 108 is formed on the surface of thecopper member 100 by theadditive agent 107 reacting with the copper. Theblack film 108 is made of, for example, a mixture of Cu2Cl2, Cu2O, and Cu3P. - In this process, it is favorable for the plating amount for the
silicon wafer 101 to be not less than (S×14) coulombs, where the surface area of the region where the surface of thecopper member 100 contacts theplating liquid 106 is S (cm2). Thereby, theblack film 108 can be reliably formed. For example, in the case where thecopper member 100 is a circular plate having a diameter of 300 mm and one face of thecopper member 100 contacts theplating liquid 106, the surface area S is about 706.5 cm2. In such a case, because 706.5×=9891, it is sufficient to perform plating of 10 kilocoulombs or more. If necessary, a plurality of thedummy silicon wafers 101 may be used sequentially. - Then, as shown in step S7 of
FIG. 2 , the quality of thecopper plating layer 110 formed on thesilicon wafer 101 is inspected. Then, if the quality is defective, the flow returns to step S6; and the plating processing of thedummy silicon wafer 101 is continued. On the other hand, if the quality is good, the flow proceeds to step S8 to transition to the main plating processing. - Continuing as shown in step S8 of
FIG. 2 andFIG. 3C , thedummy silicon wafer 101 is removed from theholder 27; and thesilicon wafer 102 for the main plating is mounted. Because, theadditive agent 107 is not supplied to the interior of theanode chamber 23 after the start of the plating processing of the dummy shown in step S6, the concentration of theadditive agent 107 of theplating liquid 106 inside theanode chamber 23 decreases as the plating processing of the dummy progresses. On the other hand, because theadditive agent 107 is supplied continuously to the interior of thecathode chamber 24 via theconduit 51, the concentration of theadditive agent 107 inside thecathode chamber 24 is substantially constant. - Then, as shown in step S9 of
FIG. 2 andFIG. 3D , copper plating of thesilicon wafer 102 is performed by thepower supply 28 again applying the voltage. At this time, although theadditive agent 107 is supplied to the interior of thecathode chamber 24 via theconduit 51, theadditive agent 107 is not supplied to the interior of theanode chamber 23. Although thecopper plating layer 110 is formed on the surface of thesilicon wafer 102 by the plating processing, the monovalent copper ions (Cu+) substantially are not produced because the surface of thecopper member 100 is covered with theblack film 108; and, accordingly, theforeign matter 112 substantially does not form. Also, theadditive agent 107 that remained inside theanode chamber 23 is consumed by the copper plating processing and substantially no longer exists. - Thus, the
copper plating layer 110 can be formed on the surface of thesilicon wafer 102 for the main plating. Then, when the plating processing of onesilicon wafer 102 ends, thesilicon wafer 102 is removed from thecopper plating apparatus 1; anew silicon wafer 102 is mounted to thecopper plating apparatus 1; and the plating processing is continued. Thus, the plating processing can be performed sequentially formultiple silicon wafers 102 until thecopper member 100 is consumed and can no longer be used. When thecopper member 100 is replaced, the main plating processing shown in step S9 is performed after re-implementing the preparation processes shown in steps S1 to S8 described above. - Then, a conductive member such as an interconnect, etc., can be formed on the
silicon wafer 102 by selectively forming thecopper plating layer 110 on thesilicon wafer 102 in step S9, or by uniformly forming thecopper plating layer 110 in step S9 and subsequently performing patterning. Thereafter, the semiconductor device can be manufactured by performing the necessary processing. - Effects of the embodiment will now be described.
- In the embodiment, the plating liquid 106 including the
additive agent 107 is supplied to the interior of theanode chamber 23 in the dummy plating process shown in step S6 ofFIG. 2 andFIG. 3B . Therefore, theblack film 108 can be formed quickly on the surface of thecopper member 100. Thereby, in the main plating process shown in step S9 ofFIG. 2 andFIG. 3D , the production of the monovalent copper ions can be suppressed; and the formation of theforeign matter 112 on thesilicon wafer 102 can be suppressed. As a result, a uniformcopper plating layer 110 can be formed on thesilicon wafer 102. Further, dust that is due to theforeign matter 112 coming off into the plating liquid 106 can be prevented from occurring. - Also, in the embodiment, after introducing a constant amount of the
additive agent 107 into theanode chamber 23 at the start of the dummy plating process, the plating processing is performed by supplying only the plating liquid 106 to the interior of theanode chamber 23 without supplying theadditive agent 107. Thereby, theblack film 108 can be prevented from being formed to be excessively thick; and theblack film 108 can be prevented from coming off and becoming dust. Also, the cost of the plating processing can be suppressed because theadditive agent 107 that is inside theanode chamber 23 is not consumed excessively. On the other hand, because theadditive agent 107 is supplied continuously to the interior of thecathode chamber 24, thecopper plating layer 110 can be formed stably. - A comparative example will now be described.
-
FIG. 4 is a graph showing the change over time of the dust count of the comparative example, where the horizontal axis is the plating processing time after placing a new copper member, and the vertical axis is the dust count. - In the comparative example, the plating processing was performed using a
new copper member 100 by supplying the plating liquid 106 not including theadditive agent 107 to the interior of theanode chamber 23 and by supplying the plating liquid 106 including theadditive agent 107 to the interior of thecathode chamber 24. - As a result, as shown in
FIG. 4 , after a constant amount of time has elapsed after the start of the plating processing, the dust count inside the plating liquid 106 greatly increases and subsequently decreases. It is considered that the increase of the dust count is because theblack film 108 is not formed on the surface of thecopper member 100, monovalent copper ions are formed, and theforeign matter 112 forms on the silicon wafer because theadditive agent 107 is not supplied to the interior of theanode chamber 23. When theforeign matter 112 forms at thecopper plating layer 110, open defects occur easily for interconnects in the case where the interconnects are formed from thecopper plating layer 110. - Further, it is considered that the reason that the dust count decreased after increasing once is because the
additive agent 107 entered theanode chamber 23 little by little via the blockingfilm 22; and thereby, theblack film 108 was formed. Therefore, it also may be considered to perform the plating processing by utilizing this phenomenon and waiting until the dust count decreases. However, in such a case, it is necessary to continue the plating processing of the dummy until theblack film 108 is formed by theadditive agent 107 leaking into theanode chamber 23 and the formation of theforeign matter 112 decreases sufficiently; and the productivity of the plating processing decreases. In an example, dummy plating processing for several days is necessary until theblack film 108 is formed by theadditive agent 107 leaking via the blockingfilm 22 and the dust count decreases. Conversely, according to the embodiment described above, transition to the main plating processing is possible when the plating processing of the dummy is performed for several minutes. - It also may be considered to not provide the blocking
film 22 and to perform the plating processing by supplying the plating liquid 106 including theadditive agent 107 to the entire interior of theplating tank 21. However, in such a case, theblack film 108 that has become too thick comes off, mixes into theplating liquid 106, and causes defects such as embedding defects, etc. Moreover, the consumption of theadditive agent 107 is high; and the cost of the plating processing increases. Further, it is necessary to frequently replace thefilters - According to the embodiment described above, a copper plating apparatus, a copper plating method, and a method for manufacturing the semiconductor device can be realized to perform inexpensive and high-precision copper plating.
- While certain embodiments have been described, these embodiments have been presented by way of example only, and are not intended to limit the scope of the inventions. Indeed, the novel embodiments described herein may be embodied in a variety of other forms; furthermore, various omissions, substitutions and changes in the form of the embodiments described herein may be made without departing from the spirit of the inventions. The accompanying claims and their equivalents are intended to cover such forms or modifications as would fall within the scope and spirit of the invention.
Claims (16)
1. A copper plating apparatus, comprising:
a plating tank configured to have a copper member and a plating member disposed in an interior of the plating tank;
a blocking film configured to partition the interior of the plating tank into an anode chamber where the copper member is to be disposed and a cathode chamber where the plating member is to be disposed, the blocking film being configured to transmit copper ions and not transmit an additive agent;
a supply unit configured to supply the additive agent to the anode chamber; and
a power supply configured to apply a voltage between the copper member and the plating member.
2. The copper plating apparatus according to claim 1 , further comprising:
an anode-side circulation water path configured to circulate plating liquid for the anode chamber; and
a cathode-side circulation water path configured to circulate plating liquid for the cathode chamber,
the supply unit being configured to supply the additive agent to the anode-side circulation water path.
3. The copper plating apparatus according to claim 1 , wherein the blocking film is an ion exchange film.
4. A copper plating method, comprising:
disposing a copper member in an anode chamber of a plating tank, supplying plating liquid including an additive agent to the anode chamber, disposing a first plating member in a cathode chamber partitioned from the anode chamber by a blocking film configured to transmit copper ions and not transmit the additive agent, and supplying the plating liquid including the additive agent to the cathode chamber;
applying a voltage to cause the copper member to be positive and the first plating member to be negative to perform copper plating on the first plating member and form a black film at a surface of the copper member;
replacing the first plating member with a second plating member after the black film is formed; and
applying a voltage to cause the copper member to be positive and the second plating member to be negative to perform copper plating on the second plating member while supplying the additive agent to the cathode chamber without supplying the additive agent to the anode chamber.
5. The copper plating method according to claim 4 , wherein the additive agent contains an accelerator configured to promote the copper plating, a suppressor configured to suppress the copper plating, and a leveler configured to level a copper plating layer.
6. The copper plating method according to claim 4 , wherein the additive agent contains polyethylene glycol.
7. The copper plating method according to claim 4 , wherein the additive agent contains bis 3-sulfopropyl disulfide disodium.
8. The copper plating method according to claim 4 , wherein a concentration of the additive agent in the plating liquid supplied to the anode chamber in the supplying of the plating liquid is not less than 1 ppm.
9. The copper plating method according to claim 4 , wherein the plating amount for the first plating member in the forming of the black film is set to be not less than (S×14) coulombs, where the surface area of a region where the surface of the copper member contacts the plating liquid is S (cm2).
10. The copper plating method according to claim 4 , wherein the second plating member is a silicon wafer.
11. A method for manufacturing a semiconductor device, comprising:
disposing a copper member in an anode chamber of a plating tank, supplying a plating liquid including an additive agent to the anode chamber, disposing a plating member in a cathode chamber partitioned from the anode chamber by a blocking film configured to transmit copper ions and not transmit the additive agent, and supplying the plating liquid including the additive agent to the cathode chamber;
applying a voltage to cause the copper member to be positive and the plating member to be negative to perform copper plating on the plating member and form a black film at a surface of the copper member;
replacing the plating member with a silicon wafer after the black film is formed; and
applying a voltage to cause the copper member to be positive and the silicon wafer to be negative to perform copper plating on the silicon wafer while supplying the additive agent to the cathode chamber without supplying the additive agent to the anode chamber.
12. The method for manufacturing the semiconductor device according to claim 11 , wherein the additive agent contains an accelerator configured to promote the copper plating, a suppressor configured to suppress the copper plating, and a leveler configured to level a copper plating layer.
13. The method for manufacturing the semiconductor device according to claim 11 , wherein the additive agent contains polyethylene glycol.
14. The method for manufacturing the semiconductor device according to claim 11 , wherein the additive agent contains bis 3-sulfopropyl disulfide disodium.
15. The method for manufacturing the semiconductor device according to claim 11 , wherein a concentration of the additive agent in the plating liquid supplied to the anode chamber in the supplying of the plating liquid is not less than 1 ppm.
16. The method for manufacturing the semiconductor device according to claim 11 , wherein the plating amount for the plating member in the forming of the black film is set to be not less than (S×14) coulombs, where the surface area of a region where the surface of the copper member contacts the plating liquid is S (cm2).
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US14/098,794 US20150068911A1 (en) | 2013-09-12 | 2013-12-06 | Copper plating apparatus, copper plating method and method for manufacturing semiconductor device |
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US201361876976P | 2013-09-12 | 2013-09-12 | |
US14/098,794 US20150068911A1 (en) | 2013-09-12 | 2013-12-06 | Copper plating apparatus, copper plating method and method for manufacturing semiconductor device |
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Cited By (1)
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JP7041795B1 (en) * | 2021-12-20 | 2022-03-24 | 株式会社荏原製作所 | How to maintain the plating equipment |
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JP7041795B1 (en) * | 2021-12-20 | 2022-03-24 | 株式会社荏原製作所 | How to maintain the plating equipment |
CN115087764A (en) * | 2021-12-20 | 2022-09-20 | 株式会社荏原制作所 | Maintenance method of plating apparatus |
WO2023119347A1 (en) * | 2021-12-20 | 2023-06-29 | 株式会社荏原製作所 | Maintenance method for plating device |
KR102549747B1 (en) * | 2021-12-20 | 2023-07-03 | 가부시키가이샤 에바라 세이사꾸쇼 | Maintenance method of plating equipment |
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