The present invention generally relates to an electrochemical deposition method for electrochemically preparing a uniform copper film on semiconductor substrate bearing a thin resistive seed layer as part of interconnect formation in ULSI (Ultra large scale integrated) circuit fabrication.
Semiconductor devices are manufactured or fabricated on semiconductor wafers using a number of different processing steps to create transistor and interconnection elements. In forming the device elements the semiconductor wafer may undergo, for example, masking, etching, and deposition processes to form the semiconductor transistors and desired electronic circuitry to connect those transistor terminals. In particular, multiple masking, ion implantation, annealing, and plasma etching, and chemical and physical vapor deposition steps can be performed to form shallow trench, transistor well, gate, poly-silicon line, and interconnection line structures such as vias and trenches.
After vias and trenches are formed, conductive materials are deposited into these structures to electrically connect the transistors underneath. Excess conductive materials are then removed to transform the conductive structures into desired circuitry. In forming conductive lines during ULSI (Ultra large scale integrated) circuit fabrication, electrochemical deposition of a metallic layer, usually copper, onto a substrate bearing a thin resistive seed layer is implemented. Such a deposition process can be used to fill via structures, trench structures, or combined structures of both. When these structures are filled, copper is continuously deposited to form a film covering the surface of the semiconductor wafer. A uniform final copper film is critical because the subsequent process step, commonly a planarization step (CMP), to remove the excess conductive copper requires a high degree of uniformity in order to achieve the equal electrical performance from device to device at the end of production line. The within film non-uniformity (WFNU), which is the ratio of the standard deviation of film thickness over the mean film thickness, is generally controlled under 2.5% in advanced process technology.
Large WFNU has a negative effect on the following CMP process step by causing either regional Cu remaining or excessive dielectric materials loss at the end of Cu polishing. If the same amount of Cu is removed evenly across the wafer during polishing, the initial thicker Cu film around the periphery of the wafer leads to Cu or barrier residue to be left there, and this incomplete removal process causes electrical short of the device. If a large amount of over-polishing is enforced to clear Cu and barrier materials on wafer periphery, the regions near wafer center surfer excessive loss of dielectric materials, thereby reducing the height of trenches and vias, which leads to different electrical resistance among the interconnection lines across the wafer. Both effects can impact device yield substantially.
As wafer size migrates to from 200 mm to 300 mm, and seed layer thickness continuously to decrease for every generation of manufacture technology that advances, ohmic resistance of the seed layer on the surface of the semiconductor wafer increases significantly. In conventional electrochemical deposition process, often referred as plating, a power source supplies electrical current or potential to a single working electrode and the wafer substrate bearing a seed layer. The wafer substrate, working electrode, power supply, and the electrolyte form an electrolytic cell. Current density across the thin resistive seed layer is non-uniform, higher at substrate periphery due to a phenomenon called “terminal effect”. This current non-uniformity results in higher plating rate at the edge of semiconductor wafer and lower plating rate at the center of semiconductor wafer, which leads to non-uniform thickness of deposited copper film on the surface of semiconductor wafer. Terminal effect is more profound with less seed layer thickness and larger wafer size. In most severe embodiments, deposition only occurs at wafer periphery.
The terminal effect can be reduced by employing an electrolyte solution with relative lower acid content, as shown in
In the earlier patents, sophisticated designs have been incorporated into processing apparatus to resolve the non-uniformity problem caused by terminal effect. U.S. Pat. No. 6,391,166 (Jan. 15, 1999) disclosed plating apparatus and methods that utilized an independent power control for a system of electrodes to overcome the non-uniform plating rate on semiconductor wafer with very thin seed layer. U.S. Pat. No. 6,755,954 (Jun. 29, 2004) disclosed an apparatus and a method for electroplating of copper film with relatively small thickness variation. It showed an example, to form a 0.6 um (6000 Å) copper film with 394 Å thickness variation on 300 mm wafer bearing a 400 Å thick seed layer.
The present invention discloses methods applied to an electrochemical deposition apparatus with multiple electrodes and a system of electrical power controls. Such an apparatus is referred as “said apparatus” throughout the text and figures in this invention. An example of such an apparatus is described in earlier U.S. Pat. No. 6,391,166 and PCT Patent Application No. PCT/CN2007/071008.
The disclosed methods apply to plating wafers bearing a seed layer with a thickness from 50 Å to 900 Å in a copper sulfate based electrolyte with conductivity ranging from 0.02 to 0.8 S/cm.
The disclosed methods produced electrochemically plated copper film with a within film non-uniformity as small as 0.33% (a variation of 42 Å) on 350 Å seed layer, several times less than what was disclosed in previous patents.
a-3d show deposition profiles from a single-electrode plating apparatus.
a and 5b illustrate waveform diagrams applied to a two-electrode plating apparatus.
a and 6b show deposition profiles from a two-electrode apparatus;
a and 8b illustrate waveform diagrams applied to a three-electrode plating apparatus.
a and 9b show deposition profiles from a three-electrode apparatus;
a and 11b illustrate waveform diagrams applied to a four-electrode plating apparatus.
a and 12b show deposition profiles from a four-electrode apparatus;
The present invention discloses methods applied to an electrochemical deposition apparatus with multiple electrodes and a system of electrical power controls. The disclosed methods apply to plating wafers bearing a seed layer with a thickness from 50 Å to 900 Å in a copper sulfate based electrolyte with conductivity ranging from 0.02 to 0.8 S/cm. The disclosed method is to be practiced on apparatus disclosed in U.S. Pat. No. 6,391,166.
The methods in present invention include the following steps:
introducing a copper sulfate based electrolyte with a flow rate in the range of 1 to 20 LPM into said apparatus;
transferring a semiconductor wafer to a semiconductor wafer holder with electrical conduction path to wafer;
applying a small bias voltage to wafer;
bringing wafer into electrolyte, and the front surface of the wafer being in full contact with the electrolyte;
applying electrical current to each electrode; the power supplying connected to electrodes switch from constant voltage mode to constant current mode at desired times;
applying current or potential at a relative small value on each of electrodes, preferably the combined current being from 2 Å to 10 Å, and the ratio of the current densities of between electrodes being from 0.5:1 to 300:1;
applying current or potential at a relative large value on each of electrodes, preferably the combined current being from 10 Å to 40 Å, and the ratio of the current densities between electrodes being from 0.5:1 to 300:1;
switching power supply to a small bias voltage mode and apply it on said semiconductor wafer;
bringing wafer out of the electrolyte.
stopping power supply and clean off the residue electrolyte on wafer surface.
The current distribution on each electrode and the ratio of current densities between electrodes in steps 6 and 7 above vary in narrower ranges depending on the number of electrodes used and the conductivity of the electrolyte. In the following embodiments, these ranges are specified for an apparatus with a particular number of electrodes and a particular electrolyte conductivity.
In one embodiment a method applied to said apparatus comprising two electrodes with electrolyte conductivity of 0.02-0.2 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising two electrodes with electrolyte conductivity of 0.2-0.8 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising three electrodes with electrolyte conductivity of 0.02-0.2 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising three electrodes with electrolyte conductivity of 0.2-0.8 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising four electrodes with electrolyte conductivity of 0.02-0.2 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising four electrodes with electrolyte conductivity of 0.2-0.8 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising ten electrodes with electrolyte conductivity of 0.02-0.2 S/cm is disclosed.
In one embodiment, a method applied to said apparatus comprising ten electrodes with electrolyte conductivity of 0.2-0.8 S/cm is disclosed.
A conventional plating apparatus with single electrode 201 is illustrated in
WFNU values calculated from the thickness profiles in
On the same 350 Å-thick seed layer, the WFNU improves when the plating thickness increases, as illustrated in
In this invention, thinner seed (350 Å) and plating thickness (3000 Å) are used for all analysis forward. This combination gives the high sensitivity of the methods disclosed.
In one embodiment of the invention, a method for uniform deposition of Cu film on the surface of semiconductor wafer practiced in the apparatus illustrated in
Step 1: open flow controllers 423a and 423b to control the flow rate in the working area for each electrode respectively; the flow rate in the working area of 401a is in the range 5 to 20 LPM and that of 401b is in the range 1 to 15 LPM. In one embodiment of the invention, the flow controllers 423a and 423b are turned on at the same time. In another embodiment of the invention, the flow controllers 423a and 423b are turned on at different times.
Step 2: transfer the semiconductor wafer bearing a seed layer to the wafer holder 421 in the apparatus; the wafer holder has an electrical conducting passage that is in contact with the seed layer of the semiconductor wafer.
Step 3: apply small bias voltage in the range of 0.01 to 10 V to said semiconductor wafer.
Step 4: bring the semiconductor wafer, held by the wafer holder, into contact with the electrolyte, until the wafer front surface is fully immersed in the electrolyte.
Step 5: apply currents to electrodes 401a and 401b and maintain a positive potential on electrode 401a and a positive or negative potential on electrode 401b (The sign of the potential on each electrode is defined relatively to wafer through the text); the working current of electrode 401a is from 5 to 20 Å, and that of electrode 401b is from 0.01 to 10 Å. The ratio of the current densities on electrode 401a to that on electrode 201b is from 1:1 to 300:1. This step lasts for 5 to 30 seconds to fill the vias and trenches on the surface of semiconductor wafer 422. In one embodiment of the invention, the power supplies connected to the electrodes 401a and 401b switch from constant voltage mode to constant current mode at the same time. In another embodiment of the invention, the power supplies connected to the electrodes 401a and 401b switch from constant voltage mode to constant current mode at different times.
Step 6: power supplies connected to electrodes 401a and 401b control a positive potential on electrode 401a and a positive or negative potential on electrode 401b; the working current on electrode 401a is from 15 to 40 Å, and that on electrode 401b is from 0.01 to 20 Å. The ratio of the current densities on electrode 401a to that on electrode 401b is from 1:1 to 300:1. This step increases the efficiency of the electrochemical deposition by applying relative large electrical currents on the electrodes 401a and 401b. This step terminates when a desired deposition thickness is achieved.
Step 7: apply a small bias voltage on said semiconductor wafer. In one embodiment of the invention, the electrodes 401a and 401b are switched from constant current mode to constant voltage mode at the same time. In another embodiment of the invention, the electrodes 401a and 401b are switched from constant current mode to constant voltage mode at different times.
Step 8: bring the semiconductor wafer out of the electrolyte and spin off the residue electrolyte left on the wafer surface.
In above step 5 and step 6, the sign of potential on electrode 401b is determined to be positive or negative based on the electrochemical deposition conditions. For example, if the conductivity of electrolyte is low and conductive layer on semiconductor wafer is thick, positive potential will be applied to both electrodes 401a and 401b as illustrated in
The detailed sets of current density ratio and the signs of potential on individual electrode used in step 5 for plating uniform copper film on a 300 mm semiconductor wafer bearing 200-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 3:
Step 6 begins when the plated thickness of Cu film reaches 1500 Å. The detailed sets current density ratio and the signs of potential on individual electrode used in step 6 for plating uniform copper film on a 300 mm semiconductor wafer bearing 200-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 4.
a and 6b show the deposition profiles of 3000 Å thick film deposited on 350 Å seed layer in low and high conductive electrolyte respectively; wherein the profiles of method 1 are obtained with the process parameters detailed in Table 3 and 4, while those of method 2 are obtained with the process parameters out of the range defined in Table 3 and 4. The WFNU values are listed in the Table 5. As shown in
Disclosed method (method 1) significantly improved WFNU, compared to conventional method (method 2) in both low and high conductivity electrolytes. In the embodiment of low conductivity electrolyte, a WFNU less than 2.5% is obtained.
In one embodiment of the invention, a method for uniform deposition of Cu film on the surface of semiconductor wafer practiced in the apparatus illustrated in
Step 1: open flow controllers 723a, 723b and 723c to control the flow rate in the working area for each electrode respectively; the flow rate in the working area of 701a is in the range 5 to 20 LPM, that of 701b is in the range 5 to 20 LPM, and that of 701c is 1 to 15 LPM. In one embodiment of the invention, the flow controllers 723a, 723b and 723c are turned on at the same time. In another embodiment of the invention, the flow controllers 723a, 723b and 723c are turned on at different times.
Step 2: transfer the semiconductor wafer bearing a seed layer to the wafer holder 721 in the apparatus; the wafer holder has an electrical conducting passage that is in contact with the seed layer of the semiconductor wafer.
Step 3: apply small bias voltage in the range of 0.01 to 10V to said semiconductor wafer;
Step 4: bring the semiconductor wafer, held by the wafer holder, into contact with the electrolyte, until the wafer front surface is fully immersed in the electrolyte;
Step 5: apply currents to electrodes 701a, 701b and 701c and maintain a positive potential on electrodes 701a, 701b and a positive or negative potential on electrode 701c; the working current of electrode 701a is from 2 to 20 Å, that of electrode 701b is from 0.01 to 20 Å, and that of electrode 701c is from 0.01 to 20 Å. The ratio of the current densities on electrode 701a to that on electrode 701b is from 1:1 to 50:1 and ratio of the current densities on electrode 701a to that on electrode 701c is from 1:1 to 300:1. This step lasts for 5 to 30 seconds to fill the vias and trenches on the surface of semiconductor wafer 722. In one embodiment of the invention, the power supplies connected to the electrodes 701a, 701b and 701c switch from constant voltage mode to constant current mode at the same time. In another embodiment of the invention, the power supplied connected to the electrodes 701a, 701b and 701c switch from constant voltage mode to constant current mode at different times.
Step 6: power supplies connected to electrodes 701a, 701b and 701c control a positive potential on electrodes 701a, 701b and a positive or negative potential on electrode 701c; the working current on electrode 701a is from 4 to 30 Å, that on electrode 701b is from 4 to 30 Å and that of electrode 701c is from 0.1 to 20 Å. The ratio of the current densities on electrode 701a to that on electrode 701b is from 1:1 to 50:1 and ratio of the current densities on electrode 701a to that on electrode 701c is from 1:1 to 300:1. This step increases the efficiency of the electrochemical deposition by applying relative large electrical currents on the electrodes 701a, 701b and 701c. This step terminates when desired deposition thickness is achieved.
Step 7: apply a small a bias voltage on said semiconductor wafer. In one embodiment of the invention, the electrodes 701a, 701b and 701c are switched from constant current mode to constant voltage mode at the same time. In another embodiment of the invention, the electrodes 701a, 701b and 701c are switched from constant current mode to constant voltage mode at different times.
Step 8: bring the semiconductor wafer out of the electrolyte and spin off the residue electrolyte left on the wafer surface.
In the above step 5 and step 6, the sign of potential on electrode 701c is determined to be positive or negative based on the electrochemical deposition conditions. For example, if the conductivity of electrolyte is low and conductive layer on semiconductor wafer is thick, positive potentials will be applied to all electrodes 701a, 701b and 701c as illustrated in
The detailed sets of current density ratio and the signs of potential on individual electrode used in step 5 for plating uniform copper film on a 300 mm semiconductor wafer bearing 150-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 6:
Step 6 begins when the plated thickness of Cu film reaches 1500 Å. The detailed sets current density ratio and the signs of potential on individual electrode used in step 6 for plating uniform copper film on a 300 mm semiconductor wafer bearing 150-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 7:
a and 9b show the deposition profiles of 3000 Å thick film deposited on 350 Å seed layer in low and high conductive electrolyte respectively; wherein the profiles of method 1 are obtained with the process parameters detailed in Table 6 and 7, while those of method 2 are obtained with the process parameters out of the range defined in Table 6 and 7. The WFNU values are listed in the Table 8. As shown in
Disclosed method (method 1) significantly improved WFNU, compared to conventional method (method 2) in both low and high conductivity electrolytes. In the embodiment of low conductivity electrolyte, a WFNU less than 2.5% is obtained.
In one embodiment of the invention, a method for uniform deposition of Cu film on the surface of semiconductor wafer practiced in the apparatus illustrated in
Step 1: open flow controllers 1023a, 1023b, 1023c and 1023d to control the flow rate in the working area for each electrode respectively; the flow rate in the working area of 1001a, 1001b and 1001c are in the range 5 to 20 LPM and that of 1001d is in the range 1 to 15 LPM. In one embodiment of the invention, the flow controllers 1023a, 1023b, 1023b and 1023c are turned on at the same time. In another embodiment of the invention, the flow controllers 1023a, 1023b, 1023b and 1023c are turned on at different times.
Step 2: transfer the semiconductor wafer bearing a seed layer to the wafer holder 1021 in the apparatus; the wafer holder has an electrical conducting passage that is in contact with the seed layer of the semiconductor wafer.
Step 3: apply small bias voltage in the range of 0.01 to 10V to said semiconductor wafer;
Step 4: bring the semiconductor wafer, held by the wafer holder, into contact with the electrolyte, until the wafer front surface is fully immersed in the electrolyte.
Step 5: apply currents to electrodes 1001a, 1001b and 1001c and maintain a positive potential on electrodes 1001a, 1001b, 1001c and a positive or negative potential on electrode 1001d; the working current of electrode 1001a is from 1 to 15 Å, that of electrode 1001b from 0.5 to 10 Å, and that of electrode 1001c and 1001d from 0.01 to 10 Å. The ratio of the current densities on electrode 1001a to that on electrode 1001b is from 0.5:1 to 10:1, that of electrode 1001a to 1010c from 0.5:1 to 50:1 and that of 1001a to 1001d from 1:1 to 300:1. This step lasts for 5 to 30 seconds to fill the vias and trenches on the surface of semiconductor wafer 1022. In one embodiment of the invention, the power supplies connected to the electrodes 1001a, 1001b, 1001b and 1001c switch from constant voltage mode to constant current mode at the same time. In another embodiment of the invention, the power supplies connected to the electrodes 1001a, 1001b, 1001b and 1001c switch from constant voltage mode to constant current mode at different times.
Step 6: power supplies connected to electrodes 1001a, 1001b and 1001c control a positive potential on electrodes 1001a, 1001b, 1001c and a positive or negative potential on electrode 1001d; the working current on electrode 1001a is from 2 to 30 Å, that on electrode 1001b and 1001c from 1 to 30 Å, and that of electrode 1001d from 0.01 to 20 Å. The ratio of the current densities on electrode 1001a to that on electrode 1001b is from 0.5:1 to 10:1, that of electrode 1001a to 1010c from 0.5:1 to 50:1 and that of 1001a to 1001d from 1:1 to 300:1. This step increases the efficiency of the electrochemical deposition by applying relative large electrical currents on the electrodes 1001a, 1001b, 1001c and 1001d. This step terminates when desired deposition thickness is achieved.
Step 7: Apply a small bias voltage on said semiconductor wafer. In one embodiment of the invention, the electrodes 1001a, 1001b, 1001b and 1001c are switched from constant current mode to constant voltage mode at the same time. In another embodiment of the invention, the electrodes 1001a, 1001b, 1001b and 1001c are switched from constant current mode to constant voltage mode at different times.
Step 8: bring the semiconductor wafer out of the electrolyte and spin off the residue electrolyte left on the wafer surface.
In above step 5 and step 6, the sign of potential on electrode 1001d is determined to be positive or negative based on the electrochemical deposition conditions. For example, if the conductivity of electrolyte is low and conductive layer on semiconductor wafer is thick, positive potentials will be applied to all electrodes 1001a, 1001b, 1001c and 1001d as illustrated in
The detailed sets of current density ratio and the signs of potential on individual electrode used in step 5 for plating uniform copper film on a 300 mm semiconductor wafer bearing 50-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 9:
Step 6 begins when the plated thickness of Cu film reaches 1500 Å. The detailed sets current density ratio and the signs of potential on individual electrode used in step 6 for plating uniform copper film on a 300 mm semiconductor wafer bearing 50-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 10:
a and 12b show the deposition profiles of 3000 Å thick film deposited on 350 Å seed layer in low and high conductive electrolyte respectively; wherein the profiles of method 1 are obtained with the process parameters in Table 9 and 10, while those of method 2 are obtained with the process parameters out of the range defined in Table 9 and 10. The WFNU values are listed in the following Table 11. As shown in
Disclosed method (method 1) significantly improved WFNU, compared to conventional method (method 2) in both low and high conductivity electrolytes. In the embodiment of low conductivity electrolyte, a WFNU less than 2.5% is obtained.
The above methods of present invention are practiced on simple electrode configurations of the apparatus disclosed in U.S. Pat. No. 6,391,166. Other applications of the method of the present invention practiced in those electrode configurations with more than four electrodes can be devised in similar way; wherein the area of the first electrode being 5%-30% of total electrodes area, and the ratio of the total area of all electrodes over the area of the semiconductor wafer is greater than 0.85.
The detailed sets of current density ratio and the signs of potential on individual electrode used for plating first 100 Å to 1500 Å copper film on a 300 mm semiconductor wafer bearing 50-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 12. In this embodiment, the plating apparatus consists of N electrodes, where N is between 5 and 15.
The detailed sets of current density ratio and the signs of potential on individual electrode used for plating the remaining portion of copper film on a 300 mm semiconductor wafer bearing 50-2000 Å thick seed layer in electrolyte with conductivity from 0.02 to 0.2 S/cm and conductivity from 0.2 to 0.8 S/cm are listed in Table 13.
WFNU improves as the number of electrodes, N, increases with methods disclosed in the present invention. The methods, when applied to an apparatus with more than one electrode, produces WFNU less than 2.5% on 300 mm wafer with a seed layer as thin as 350 Å. When N is increased to four, the WFNU improves to 0.33% on the same wafer and same seed layer.
The method disclosed in the present invention is compared to a method disclosed previously in U.S. Pat. No. 6,755,954. All conditions are held to be exactly the same: (1) multiple electrodes configuration (2) electrolyte conductivity=0.5 S/cm, (3) seed layer thickness=400 Å, (4) total plating thickness=6000 Å, and (5) excluding 2.7 mm of Cu film from wafer edge. To make direct comparison, thickness uniformity range values are used, instead of WFNU values.
The method of present invention produces a deposited film with WFNU=0.72% and thickness uniformity range=138.4 Å, nearly 2× improvement compared to the disclosed method in U.S. Pat. No. 6,755,954.
This application is a continuation-in-part of U.S. application Ser. No. 09/232,864, filed on Jan. 15, 1999 now U.S. Pat. No. 6,391,166; which claims the benefit of earlier filed U.S. Provisional Application Ser. No. 60/074,466, filed on Feb. 12, 1998, and U.S. Provisional Application Ser. No. 60/094,215, filed on Jul. 27, 1998; and this application claims the benefit of PCT. International Patent Application No. PCT/CN2007/071008, filed on Nov. 2, 2007; the entire contents of which are incorporated herein by reference.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/CN2008/072373 | 9/16/2008 | WO | 00 | 5/26/2011 |