1. Field of the Invention
The present invention relates to a plating apparatus and a plating method, and more particularly to a plating apparatus and a plating method used for filling a fine circuit pattern formed in a substrate, such as a semiconductor substrate, with metal (interconnect material) such as copper so as to form interconnects.
2. Description of the Related Art
Recently, there has been employed a circuit forming method comprising forming fine recesses for interconnects, such as trenches or via holes in a circuit form, in a semiconductor substrate, embedding the fine recesses with copper (interconnect material) by copper plating, and removing a copper layer (plated film) at portions other than the fine recesses by CMP means or the like. In this method, from the viewpoint of reducing loads on subsequent CMP, it is desirable that a copper plated film be deposited selectively in trenches or via holes in a circuit form, and that the amount of copper plated film deposited on portions other than the trenches or via holes be small. In order to achieve such an object, there have heretofore been proposed various ideas regarding a plating solution, such as composition in a bath of a plating solution or a brightener used in a plating solution.
A plating apparatus having the following configuration has been known as this type of plating apparatus used for plating to form fine interconnects having high aspect ratios. A substrate is held in such a state that a surface (surface to be plated) of the substrate faces upward (in a face-up manner). A cathode electrode is brought into contact with a peripheral portion of the substrate so that the surface of the substrate serves as a cathode. An anode is disposed above the substrate. While a space between the substrate and the anode is filled with a plating solution, a plating voltage is applied between the substrate (cathode) and the anode to plate a surface (surface to be plated) of a substrate (for example, see Japanese laid-open patent publication No. 2002-506489).
In a plating apparatus in which a substrate is held and plated in single wafer processing while a surface of the substrate faces upward, a distribution of a plating current can be made more uniform over an entire surface of the substrate to improve uniformity of a plated film over the surface of the substrate. Generally, the substrate is transferred and subjected to various processes in such a state that a surface of the substrate faces upward. Accordingly, it is not necessary to turn the substrate at the time of plating.
Meanwhile, in order to deposit a copper plated film selectively in trenches in a circuit form or the like, there has been known a method of bringing a porous member into contact with a substrate such as a semiconductor wafer, and plating the substrate while relatively moving the porous member in a contact direction (for example, see Japanese laid-open patent publication No. 2000-232078).
However, in the prior art, when plating is performed, the amount of plated material is different in regions of the surface of the substrate depending on the shape of the interconnect pattern under the influence of distribution of current density or the influence of additives, and hence it is difficult to form a plated film having a uniform thickness over the entire surface of the substrate. For example, a plated film deposited on an interconnect section having a dense fine interconnect pattern is thicker than a plated film deposited on other portions, and a phenomenon called an overplating phenomenon generally occurs. On the other hand, the amount of plated material deposited on an interconnect section having a wide interconnect pattern is generally smaller than that on other portions. As a result, in a case where an interconnect pattern is filled entirely with interconnect material such as copper by plating, the thickness of a plated film differs depending on the locations. When plating is performed according to such method, more amount of plated material than necessary is deposited, and hence low material cost increases and a longer period of plating time is required. Further, loads on a polishing process after plating increase, and in the next generation in which a low-k material is used as an interlayer dielectric, a polishing apparatus will require a considerably high performance.
In order to solve the above problems, there have been proposed various ideas or attempts regarding a plating solution such as composition in a bath of the plating solution or a brightener used in a plating solution, and improvement of current condition. These ideas or attempts can achieve the object to a certain extent but have a limitation such as a plated film of poor quality.
The present invention has been made in view of the above circumstances. It is therefore an object of the present invention to provide a plating apparatus and a plating method which can easily form a plated film having a flat surface and a good quality.
According to a first aspect of the present invention, there is provided a plating apparatus comprising: a substrate stage for holding a substrate; a cathode unit having a seal member for hermetically sealing a peripheral portion of a surface, to be plated, of the substrate by contacting the peripheral portion of the surface, to be plated, of the substrate held by the substrate stage, and a cathode electrode which is brought into contact with the substrate to supply current to the substrate; an electrode head disposed so as to face the surface, to be plated, of the substrate and be movable toward and away from the surface to be plated, and having an anode and a porous member with water retentivity at upper and lower parts of the electrode head; a pressing mechanism for pressing the porous member against the surface, to be plated, of the substrate held by the substrate stage under a desired pressure; and a driving mechanism for making a relative motion between the porous member and the substrate while the porous member and the surface, to be plated, of the substrate held by the substrate stage are brought into contact with each other.
According to the present invention, while the porous member and the surface, to be plated, of the substrate held by the substrate stage are brought into contact with each other, the porous member and the substrate make a relative motion, and then plating is performed, whereby plating can be suppressed in the upper part of the interconnect pattern for thereby lowering a plating rate. Thus, the plating rate in the upper part of the interconnect pattern is smaller than that in the inner part of the interconnect pattern, and the height of a plated film in the inner part of the interconnect pattern is allowed to catch up with the height of a plated film in the upper part of the interconnect pattern regardless of variations of the shape of the interconnect pattern, and hence the plated film whose surface is flat can be formed. Further, special current condition and special additives are not necessary, and the surface of the plated film is not required to be shaved, and thus the plated film of good quality can be obtained.
According to a preferred aspect of the present invention, the relative motion is a rotary motion. At least one of the porous member and the substrate held by the substrate stage is rotated, and thus the relative motion can be performed by a rotary motion.
According to a preferred aspect of the present invention, the relative motion is a scroll motion. At least one of the porous member and the substrate held by the substrate stage makes a scroll motion, i.e. makes an orbital motion (translational rotary motion) without rotation on its axis, and thus the relative motion can be performed by the scroll motion.
According to a preferred aspect of the present invention, the center of the porous member is displaced from the center of the substrate held by the substrate stage, and the porous member and the substrate rotate about their respective centers.
According to a preferred aspect of the present invention, the relative motion is a linear motion. The relative motion comprising the linear motion may be performed in such a manner that one of the porous member and the substrate held by the substrate stage may be stationary and the other may make a linear motion, or both of the porous member and the substrate may make linear motions in opposite directions.
According to a second aspect of the present invention, there is provided a plating apparatus comprising: a substrate stage for holding a substrate; a cathode unit having a seal member for hermetically sealing a peripheral portion of a surface, to be plated, of the substrate by contacting the peripheral portion of the surface, to be plated, of the substrate held by the substrate stage, and a cathode electrode which is brought into contact with the substrate to supply current to the substrate; an electrode head disposed so as to face the surface, to be plated, of the is substrate and be movable toward and away from the surface to be plated, and having an anode and a porous member with water retentivity at upper and lower parts of the electrode head; a pressing mechanism for pressing the porous member against the surface, to be plated, of the substrate held by the substrate stage under a desired pressure; and a driving mechanism for making a relative motion between the porous member and the substrate held by the substrate stage so that contact and non-contact between the porous member and the surface, to be plated, of the substrate are repeated.
With the above arrangement, the porous member and the substrate held by the substrate stage make a relative motion so that contact and non-contact between the porous member and the surface, to be plated, of the substrate are repeated, and then plating is performed. In this case also, plating can be suppressed in the upper part of the interconnect pattern for thereby lowering a plating rate, and the plating rate in the upper part of the interconnect pattern is smaller than that in the inner part of the interconnect pattern, and hence a plated film whose surface is flat can be formed.
According to a third aspect of the present invention, there is provided a plating method comprising: placing a porous member having water retentivity between a substrate and an anode; filling a plating solution between the substrate and the anode; making a relative motion between the porous member and the surface, to be plated, of the substrate while the porous member and the surface, to be plated, of the substrate are brought into contact with each other; and plating the substrate by flowing current between the substrate and the anode.
According to a preferred aspect of the present invention, the plating is performed by starting of the flowing current within two seconds after the relative motion. In this manner, after the relative motion between the porous member and the substrate is made while the porous member and the substrate are brought into contact with each other, plating is started within two seconds by flowing current. Thus, the ratio of the plating rate in the inner part of the interconnect pattern to the plating rate in the upper part of the interconnect pattern (plating rate in the inner part of the interconnect pattern/plating rate in the upper part of the interconnect pattern) can be two or more times, for example.
According to a preferred aspect of the present invention, the relative motion is a rotary motion.
According to a preferred aspect of the present invention, the relative motion is a scroll motion.
According to a preferred aspect of the present invention, the center of the porous member is displaced from the center of the substrate held by the substrate stage, and the porous member and the substrate rotate about their respective centers.
According to a preferred aspect of the present invention, the relative motion is a linear motion.
According to a fourth aspect of the present invention, there is provided a plating method comprising: placing a porous member having water retentivity between a substrate and an anode; filling a plating solution between the substrate and the anode; making a relative motion between the porous member and the surface, to be plated, of the substrate so that contact and non-contact between the porous member and the surface, to be plated, of the substrate are repeated; and plating the substrate by flowing current between the substrate and the anode.
According to a preferred aspect of the present invention, the plating is performed by starting of the flowing current within two seconds after the relative motion.
A plating apparatus and a plating method according to embodiments of the present invention will be described below with reference to the drawings. The following embodiments show examples in which copper as an interconnect material is embedded in fine recesses for interconnects formed in a surface of a substrate such as a semiconductor wafer so as to form interconnects composed of a copper layer. However, it should be noted that other kinds of interconnect materials may be used instead of copper.
Then, as shown in
Then, as shown in
The frame 12 is shielded so as not to allow a light to transmit therethrough, thereby enabling subsequent processes to be performed under a light-shielded condition in the frame 12. Specifically, the subsequent processes can be performed without irradiating the interconnects with a light such as an illuminating light. By thus preventing the interconnects from being irradiated with a light, it is possible to prevent the interconnects of copper from being corroded due to a potential difference of light that is caused by application of light to the interconnects composed of copper, for example.
In this embodiment, the electrode head 502 whose diameter is slightly smaller than that of the substrate stage 504 is used so that plating can be performed over the substantially entire surface, to be plated, of the substrate W without changing a relative position between the electrode head 502 and the substrate stage 504.
In this embodiment, the present invention is applied to a so-called face-up type plating apparatus in which the substrate is held and plated in such a state that the front face of the substrate faces upwardly. However, the present invention is applicable to a so-called face-down type plating apparatus in which the substrate is held and plated in such a state that a front face of the substrate faces downwardly, or a so-called vertical-set type plating apparatus in which the substrate is held in a vertical direction and plated.
An annular vacuum attraction groove 504b communicating with a vacuum passage 504a provided in the substrate stage 504 is formed in a peripheral portion of an upper surface of the substrate stage 504. Seal rings 508 and 510 are provided on inward and outward sides of the vacuum attraction groove 504b, respectively. With the above structure, the substrate W is placed on the upper surface of the substrate stage 504, and the vacuum attraction groove 504b is evacuated through the vacuum passage 504a to attract the peripheral portion of the substrate W, thereby holding the substrate W.
An elevating/lowering motor (not shown) comprising a servomotor and a ball screw (not shown) are used to move the swing arm 500 vertically, and a swinging motor (not shown) is used to rotate (swing) the swing arm 500. Alternatively, a pneumatic actuator may be used instead of the motor.
In this embodiment, the cathode unit 506 has the cathode electrodes 512 comprising six cathode electrodes, and the annular seal member 514 disposed above the cathode electrodes 512 so as to cover upper surfaces of the cathode electrodes 512. The seal member 514 has an inner circumferential portion which is inclined inwardly and downwardly so that a thickness of the seal member 514 is gradually reduced. The seal member 514 has an inner circumferential edge portion extending downwardly. With this structure, when the substrate stage 504 is moved upwardly, the peripheral portion of the substrate W held by the substrate stage 504 is pressed against the cathode electrodes 512, thus flowing current to the substrate W. At the same time, the inner circumferential edge portion of the seal member 514 is held in close contact with the upper surface of the peripheral portion of the substrate W to seal a contact portion hermetically. Accordingly, a plating solution that has been supplied onto the upper surface (surface to be plated) of the substrate W is prevented from leaking from the end portion of the substrate W, and the cathode electrodes 512 are thus prevented from being contaminated by the plating solution.
In this embodiment, the cathode unit 506 is not movable vertically, but is rotatable together with the substrate stage 504. However, the cathode unit 506 may be designed to be movable vertically so that the seal member 514 is brought into close contact with the surface, to be plated, of the substrate W when the cathode unit 506 is moved downwardly.
The above-mentioned electrode head 502 comprises a rotatable housing 522 and a vertically movable housing 520 which have a bottomed cylindrical shape with a downwardly open end and are disposed concentrically. The rotatable housing 522 is fixed to a lower surface of a rotating member 524 attached to a free end of the swing arm 500 so that the rotatable housing 522 is rotated together with the rotating member 524. An upper portion of the vertically movable housing 520 is positioned inside the rotatable housing 522, and the vertically movable housing 520 is rotated together with the rotatable housing 522 and is moved relative to the rotatable housing 522 in a vertical direction. The vertically movable housing 520 defines an anode chamber 530 by closing the lower open end of the vertically movable housing 520 with a porous member 528 so that a circular anode 526 is disposed in the anode chamber 530 and is dipped in a plating solution Q which is introduced to the anode chamber 530.
In this embodiment, the porous member 528 has a multi-layered structure comprising three-layer laminated porous materials. Specifically, the porous member 528 comprises a plating solution impregnated material 532 serving to hold a plating solution mainly, and a porous pad 534 attached to a lower surface of the plating solution impregnated material 532. This porous pad 534 comprises a lower pad 534a adapted to be brought into direct contact with the substrate W, and an upper pad 534b disposed between the lower pad 534a and the plating solution impregnated material 532. The plating solution impregnated material 532 and the upper pad 534b are positioned in the vertically movable housing 520, and the lower open end of the vertically movable housing 520 is closed by the lower pad 534a.
As described above, since the porous member 528 has a multi-layered structure, it is possible to use the porous pad 534 (the lower pad 534a) which contacts the substrate W, for example, and has flatness enough to flatten irregularities on the surface, to be plated, of the substrate W.
The lower pad 534a is required to have the contact surface adapted to contact the surface (surface to be contacted) of the substrate W and having a certain degree of flatness, and to have fine through-holes therein for allowing the plating solution to pass therethrough. It is also necessary that at least the contact surface of the lower pad 534a is made of an insulator or a material having high insulating properties. The surface of the lower pad 534a is required to have a maximum roughness (RMS) of about several tens μm or less.
It is desirable that the fine through-holes of the lower pad 534a have a circular cross section in order to maintain flatness of the contact surface. An optimum diameter of each of the fine through-holes and the optimum number of the fine through-holes per unit area vary depending on the kind of a plated film and an interconnect pattern. However, it is desirable that both the diameter and the number are as small as possible in view of improving selectivity of a plated film which is growing in a recess. Specifically, the diameter of each of the fine through-holes may be not more than 30 μm, preferably in the range of 5 to 20 μm. The number of the fine through-holes having such diameter per unit area may be represented by a porosity of not more than 50%.
Further, it is desirable that the lower pad 534a has a certain degree of hardness. For example, the lower pad 534a may have a tensile strength ranging from 5 to 100 kg/cm2 and a bend elastic constant ranging from 200 to 10000 kg/cm2.
Furthermore, it is desirable that the lower pad 534a is made of hydrophilic material. For example, the following materials may be used after being subjected to hydrophilization or being introduced with a hydrophilic group by polymerization. Examples of such materials include porous polyethylene (PE), porous polypropylene (PP), porous polyamide, porous polycarbonate, and porous polyimide. The porous PE, the porous PP, the porous polyamide, and the like are produced by using fine powder of ultrahigh-molecular polyethylene, polypropylene, and polyamide, or the like as a material, squeezing the fine powder, and sintering and forming the squeezed fine powder. These materials are commercially available. For example, “Furudasu S (tradename)” manufactured by Mitsubishi Plastics, Inc, “Sunfine UF (trade name)”, “Sunfine AQ (trade name)”, both of which are manufactured by Asahi Kasei Corporation, and “Spacy (trade name)” manufactured by Spacy Chemical Corporation are available on the market. The porous polycarbonate may be produced by passing a high-energy heavy metal such as copper, which has been accelerated by an accelerator, through a polycarbonate film to form straight tracks, and then selectively etching the tracks.
The lower pad 534a may be produced by a flattening process in which the surface, to be brought into contact with the surface of the substrate W, of the lower pad 534a is compacted or machined to a flat finish for thereby enabling a high-preferential deposition in the fine recesses.
On the other hand, the plating solution impregnated material 532 is composed of porous ceramics such as alumina, SiC, mullite, zirconia, titania or cordierite, or a hard porous member such as a sintered compact of polypropylene or polyethylene, or a composite material comprising these materials. In case of the alumina-based ceramics, for example, the ceramics with a pore diameter of 30 to 200 μm is used. In case of the SiC, SiC with a pore diameter of not more than 30 μm, a porosity of 20 to 95%, and a thickness of about 1 to 20 mm, preferably 5 to 20 mm, more preferably 8 to 15 mm, is used. The plating solution impregnated material 532, in this embodiment, is composed of porous ceramics of alumina having a porosity of 30%, and an average pore diameter of 100 μm. The porous ceramic plate per se is an insulator, but is constructed so as to have a smaller conductivity than the plating solution by causing the plating solution to enter its inner part complicatedly and follow a considerably long path in the thickness direction.
In this manner, the plating solution impregnated material 532 is disposed in the anode chamber 530, and generates high resistance. Hence, the influence of the resistance of the copper layer 7 (see
The electrode head 502 has a pressing mechanism comprising an air bag 540 in this embodiment for pressing the lower pad 534a against the surface (surface to be plated) of the substrate W held by the substrate stage 504 under a desired pressure. Specifically, in this embodiment, a ring-shaped air bag (pressing mechanism) 540 is provided between the lower surface of the top wall of the rotatable housing 522 and the upper surface of the top wall of the vertically movable housing 520, and this air bag 540 is connected to a pressurized fluid source (not shown) through a fluid introduction pipe 542.
Thus, the swing arm 500 is fixed at a predetermined position (process position) so as not to move vertically, and then the inner part of the air bag 540 is pressurized under a pressure of P, whereby the lower pad 534a is uniformly pressed against the surface (surface to be plated) of the substrate W held by the substrate stage 504 under a desired pressure. Thereafter, the pressure P is restored to an atmospheric pressure, whereby pressing of the lower pad 534a against the substrate W is released.
A plating solution introduction pipe 544 is attached to the vertically movable housing 520 to introduce the plating solution into the vertically movable housing 520, and a pressurized fluid introduction pipe (not shown) is attached to the vertically movable housing 520 to introduce a pressurized fluid into the vertically movable housing 520. A number of pores 526a are formed within the anode 526. Thus, a plating solution Q is introduced from the plating solution introduction pipe 544 into the anode chamber 530, and the inner part of the anode chamber 530 is pressurized, whereby the plating solution Q reaches the upper surface of the plating solution impregnated material 532 through the pores 526a of the anode 526, and reaches the upper surface of the substrate W held by the substrate stage 504 through the inner part of the plating solution impregnated material 532 and inner part of the porous pad 534 (the upper pad 534b and the lower pad 534a).
The anode chamber 530 includes gases generated by chemical reaction therein, and hence the pressure in the anode chamber 530 may be varied. Therefore, the pressure in the anode chamber 530 is controlled to a certain set value by a feedback control in the process.
For example, in the case of performing copper plating, in order to suppress slime formation, the anode 526 is made of copper (phosphorus-containing copper) containing 0.03 to 0.05% of phosphorus. The anode 526 may comprise an insoluble metal such as platinum or titanium or an insoluble electrode comprising metal on which platinum or the like is plated. Since replacement or the like is unnecessary, the insoluble metal or the insoluble electrode is preferable. Further, the anode 526 may be a net-like anode which allows a plating solution to pass therethrough easily.
The cathode electrodes 512 are electrically connected to a cathode of a plating power source 550, and the anode 526 is electrically connected to an anode of the plating power source 550.
Next, operation for conducting plating by the plating apparatus will be described. First, in a state that the substrate W is attracted to and held by the upper surface of the substrate stage 504, the substrate stage 504 is raised to bring the peripheral portion of the substrates into contact with the cathode electrodes 512, thus making it possible to supply current to the substrate W. Then, the substrate stage 504 presses the seal member 514 against the upper surface of the peripheral portion of the substrate W, thereby hermetically sealing the peripheral portion of the substrate W.
On the other hand, the electrode head 502 is moved from a position (idling position) where replacement of the plating solution, removal of bubbles, and the like are conducted by idling to a predetermined position (process position) in such a state that the plating solution Q is held inside the electrode head 502. Specifically, the swing arm 500 is once raised and further swung, whereby the electrode head 502 is located immediately above the substrate stage 504. Thereafter, the electrode head 502 is lowered, and when the electrode head 502 reaches the predetermined position (process position), the electrode head 502 is stopped. Then, the anode chamber 530 is pressurized, and the plating solution Q held by the electrode head 502 is discharged from the lower surface of the porous pad 534. Next, the lower pad 534a is pressed downwardly by introducing a pressurized air into the air bag 540 to press the lower pad 534a against the upper surface (surface to be plated) of the substrate W held by the substrate stage 504 under a desired pressure.
In such a state that the lower pad 534a is brought into contact with the surface of the substrate W, the lower pad 534a is rubbed against the surface of the substrate W by making two revolutions of the lower pad 534a at a speed of 1 revolution/second, for example, and then rotation of the lower pad 534a is stopped. Alternatively, the lower pad 534a may be stationary, and the substrate W may be rotated. After rotation of the lower pad 534a is stopped, preferably within two seconds, the cathode electrodes 512 are electrically connected to the cathode of the plating power source 550 and the anode 526 is electrically connected to the anode of the plating power source 550, whereby plating starts to be performed on the surface, to be plated, of the substrate W.
In this manner, while the lower pad 534a constituting the porous member 528 is brought into contact with the surface, to be plated, of the substrate W held by the substrate stage 504, the lower pad 534a and the substrate W make a relative motion, and then plating is performed, whereby plating can be suppressed in the upper part of the interconnect pattern for thereby lowering a plating rate. Specifically,
In this manner, the relative motion between the lower pad 534a and the substrate W is made, plating is started after the termination of the relative motion, preferably within two seconds, and the plating rate in the upper part of the interconnect pattern is smaller than that in the inner part of the interconnect pattern. Thus, the height of a plated film in the inner part of the interconnect pattern is allowed to catch up with the height of a plated film in the upper part of the interconnect pattern regardless of variations of the shape of the interconnect pattern, and hence the plated film whose surface is flat can be formed. Further, special current condition and special additives are not necessary, and the surface of the plated film is not required to be shaved, and thus the plated film of good quality can be obtained.
After plating is performed for a certain period of time, the cathode electrodes 512 and the anode 526 are disconnected from the plating power source 550, and the anode chamber 530 is restored to an atmospheric pressure, and further the air bag 540 is restored to an atmospheric pressure, whereby pressing of the lower pad 534a against the substrate W is released. Then, the electrode head 502 is raised.
The above operation is repeated predetermined times, if necessary, and the copper layer 7 (see
In the above embodiments, while the lower pad 534a constituting the porous member 528 and the substrate W held by the substrate stage 504 (see
According to this embodiment, the lower pad 534a and the substrate W held by the substrate stage 504 make a relative motion so that contact and non-contact between the lower pad 534a and the surface, to be plated, of the substrate W are repeated, and then plating is performed. In this embodiment also, plating can be suppressed in the upper part of the interconnect pattern for thereby lowering a plating rate, and the plating rate in the upper part of the interconnect pattern is smaller than that in the inner part of the interconnect pattern, and hence a plated film whose surface is flat can be formed.
The plating solution which has flowed into the reservoir 604 is introduced into the plating solution regulating tank 608 by operating a pump 606. This plating solution regulating tank 608 is provided with a temperature controller 610, and a plating solution analyzing unit 612 for sampling the plating solution and analyzing the sample solution. Further, component replenishing pipes 614 for replenishing the plating solution with components which are found to be insufficient by an analysis performed by the plating solution analyzing unit 612 are connected to the plating solution regulating tank 608. When a pump 616 is operated, the plating solution in the plating solution regulating tank 608 flows in the plating solution supply pipe 618, passes through the filter 620, and is then returned to the plating solution tray 600.
In this manner, the composition and temperature of the plating solution is adjusted to be constant in the plating solution regulating tank 608, and the adjusted plating solution is supplied to the electrode head 502 of the plating apparatus 18. Then, by holding the adjusted plating solution by the electrode head 502, the plating solution having constant composition and temperature at all times can be supplied to the electrode head 502 of the plating apparatus 18.
The substrate stage 422 is coupled to an upper end of a spindle 426 which is rotated at a high speed by energization of a spindle rotating motor (not shown). Further, a cleaning cup 428 for preventing a treatment liquid from being scattered around is disposed around the substrate W held by the clamp mechanism 420, and the cleaning cup 428 is vertically moved by actuation of a cylinder (not shown).
Further, the cleaning and drying apparatus 20 comprises a chemical liquid nozzle 430 for supplying a treatment liquid to the surface of the substrate W held by the clamp mechanism 420, a plurality of pure water nozzles 432 for supplying pure water to the backside surface of the substrate W, and a pencil-type cleaning sponge 434 which is disposed above the substrate W held by the clamp mechanism 420 and is rotatable. The pencil-type cleaning sponge 434 is attached to a free end of a swing arm 436 which is swingable in a horizontal direction. Clean air introduction ports 438 for introducing clean air into the apparatus are provided at the upper part of the cleaning and drying apparatus 20.
With the cleaning and drying apparatus 20 having the above structure, the substrate W is held by the clamp mechanism 420 and is rotated by the clamp mechanism 420, and while the swing arm 436 is swung, a treatment liquid is supplied from the chemical liquid nozzle 430 to the cleaning sponge 434, and the surface of the substrate W is rubbed with the pencil-type cleaning sponge 434, thereby cleaning the surface of the substrate W. Further, pure water is supplied to the backside surface of the substrate W from the pure water nozzles 432, and the backside surface of the substrate W is simultaneously cleaned (rinsed) by the pure water ejected from the pure water nozzles 432. Thus cleaned substrate W is spin-dried by rotating the spindle 426 at a high speed.
The width of movement L of the edge nozzle 926 is set such that the edge nozzle 926 can be arbitrarily positioned in a direction toward the center from the outer peripheral end surface of the substrate, and a set value for L is inputted, according to the size, usage, or the like of the substrate W. Normally, an edge cut width C is set in the range of 2 mm to 5 mm. In the case where a rotational speed of the substrate is a certain value or higher at which the amount of liquid migration from the backside to the face is not problematic, the copper layer, and the like within the edge cut width C can be removed.
Next, the method of cleaning with this bevel etching and backside cleaning apparatus 22 will be described. First, the substrate is horizontally rotated integrally with the substrate stage 922, with the substrate being held horizontally by the spin chucks 921 of the substrate stage 922. In this state, an acid solution is supplied from the center nozzle 924 to the central portion of the face of the substrate W. The acid solution may be a non-oxidizing acid, and hydrofluoric acid, hydrochloric acid, sulfuric acid, citric acid, oxalic acid, or the like is used. On the other hand, an oxidizing agent solution is supplied continuously or intermittently from the edge nozzle 926 to the peripheral edge portion of the substrate W. As the oxidizing agent solution, one of an aqueous solution of ozone, an aqueous solution of hydrogen peroxide, an aqueous solution of nitric acid, and an aqueous solution of sodium hypochlorite is used, or a combination of these is used.
In this manner, the copper layer, or the like formed on the upper surface and end surface in the region of the edge cut width C of the substrate W is rapidly oxidized with the oxidizing agent solution, and is simultaneously etched with the acid solution supplied from the center nozzle 924 and spread on the entire face of the substrate, whereby it is dissolved and removed. By mixing the acid solution and the oxidizing agent solution at the peripheral edge portion of the substrate, a steep etching profile can be obtained, in comparison with a mixture of them which is produced in advance being supplied. At this time, the copper etching rate is determined by their concentrations. If a natural oxide film of copper is formed in the circuit-formed portion on the face of the substrate, this natural oxide is immediately removed by the acid solution spreading on the entire face of the substrate according to rotation of the substrate, and does not grow any more. After the supply of the acid solution from the center nozzle 924 is stopped, the supply of the oxidizing agent solution from the edge nozzle 926 is stopped. As a result, silicon exposed on the surface is oxidized, and deposition of copper can be suppressed.
On the other hand, an oxidizing agent solution and a silicon oxide film etching agent are supplied simultaneously or alternately from the back nozzle 928 to the central portion of the backside of the substrate. Therefore, copper or the like adhering in a metal form to the backside of the substrate W can be oxidized with the oxidizing agent solution, together with silicon of the substrate, and can be etched and removed with the silicon oxide film etching agent. This oxidizing agent solution is preferably the same as the oxidizing agent solution supplied to the face, because the types of chemicals are decreased in number. Hydrofluoric acid can be used as the silicon oxide film etching agent, and if hydrofluoric acid is used as the acid solution on the face of the substrate, the types of chemicals can be decreased in number Thus, if the supply of the oxidizing agent is stopped first, a hydrophobic surface is obtained. If the etching agent solution is stopped first, a water-saturated surface (a hydrophilic surface) is obtained, and thus the backside surface can be adjusted to a condition that will satisfy the requirements of a subsequent process.
In this manner, the acid solution, i.e., etching solution is supplied to the substrate W to remove metal ions remaining on the surface of the substrate W. Then, pure water is supplied to replace the etching solution with pure water and remove the etching solution, and then the substrate is dried by spin-drying. In this way, removal of the copper layer in the edge cut width C at the peripheral edge portion on the face of the substrate, and removal of copper contaminants on the backside are performed simultaneously to thus allow this treatment to be completed, for example, within 80 seconds. The etching cut width of the edge can be set arbitrarily (from 2 to 5 mm), but the time required for etching does not depend on the cut width.
The gas introduction pipe 1010 is connected to a mixed gas introduction line 1022 which in turn is connected to a mixer 1020 where a N2 gas introduced through a N2 gas introduction line 1016 containing a filter 1014a, and a H2 gas introduced through a H2 gas introduction line 1018 containing a filter 1014b, are mixed to form a mixed gas which flows through the line 1022 into the gas introduction pipe 1010.
In operation, the substrate W, which has been carried in the chamber 1002 through the gate 1000, is held on the elevating pins 1008 and the elevating pins 1008 are raised up to a position at which the distance between the substrate W held on the lifting pins 1008 and the hot plate 1004 becomes about 0.1 to 1.0 mm, for example. In this state, the substrate W is then heated to e.g. 400° C. through the hot plate 1004 and, at the same time, the antioxidant gas is introduced from the gas introduction pipe 1010 and the gas is allowed to flow between the substrate W and the hot plate 1004 while the gas is discharged from the gas discharge pipe 1012, thereby annealing the substrate W while preventing its oxidation. The annealing treatment may be completed in about several tens of seconds to 60 seconds. The heating temperature of the substrate may be selected in the range of 100 to 600° C.
After the completion of the annealing, the elevating pins 1008 are lowered down to a position at which the distance between the substrate W held on the elevating pins 1008 and the cool plate 1006 becomes 0 to 0.5 mm, for example. In this state, by introducing cooling water into the cool plate 1006, the substrate W is cooled by the cool plate to a temperature of 100° C. or lower in about 10 to 60 seconds. The cooled substrate is transferred to the next step.
A mixed gas of N2 gas with several percentages of H2 gas is used as the above antioxidant gas. However, N2 gas may be used singly.
As shown in
Linear guides 76, which extend vertically and guide vertical movement of the movable frame 54, are mounted to the fixed frame 52, so that by the actuation of a head-elevating cylinder (not shown), the movable frame 54 moves vertically by the guide of the linear guides 76.
Substrate insertion windows 56a for inserting the substrate W into the housing portion 56 are formed in the circumferential wall of the housing portion 56 of the processing head 60. Further, as shown in
On the other hand, a substrate fixing ring 86 is fixed to a peripheral portion of the lower surface of the substrate holder 58. A columnar pusher 90 protrudes downwardly from the lower surface of the substrate fixing ring 86 by the elastic force of a spring 88 disposed within the substrate fixing ring 86 of the substrate holder 58. Further, a flexible cylindrical bellows-like plate 92 made of e.g. Teflon (registered trademark) is disposed between the upper surface of the substrate holder 58 and the upper wall of the housing portion 56 to hermetically seal the inner part of the housing portion.
When the substrate holder 58 is in a raised position, a substrate W is inserted from the substrate insertion window 56a into the housing portion 56. The substrate W is then guided by a tapered surface 82a provided in the inner circumferential surface of the guide frame 82, and positioned and placed at a predetermined position on the upper surface of the seal ring 84a. In this state, the substrate holder 58 is lowered so as to bring the pusher 90 of the substrate fixing ring 86 into contact with the upper surface of the substrate W. The substrate holder 58 is further lowered so as to press the substrate W downwardly by the elastic force of the spring 88, thereby forcing the seal ring 84a to make pressure contact with a peripheral portion of the front surface (lower surface) of the substrate W to seal the peripheral portion while nipping the substrate W between the housing portion 56 and the substrate holder 58 to hold the substrate W.
When the head-rotating servomotor 62 is driven while the substrate W is thus held by the substrate holder 58, the output shaft 64 and the vertical shaft 68 inserted in the output shaft 64 rotate together via the spline 66, whereby the substrate holder 58 rotates together with the housing portion 56.
At a position below the processing head 60, there is provided an upward-open treatment tank 100 comprising an outer tank 100a and an inner tank 100b which have a slightly larger inner diameter than the outer diameter of the processing head 60. A pair of leg portions 104, which is mounted to a lid 102, is rotatably supported on the outer circumferential portion of the treatment tank 100. Further, a crank 106 is integrally coupled to each leg portion 106, and the free end of the crank 106 is rotatably coupled to the rod 110 of a lid-moving cylinder 108. Thus, by the actuation of the lid-moving cylinder 108, the lid 102 moves between a treatment position at which the lid 102 covers the top opening of the treatment tank 100 and a retreat position beside the treatment tank 100. In the surface (upper surface) of the lid 102, there is provided a nozzle plate 112 having a large number of jet nozzles 112a for jetting outwardly (upwardly), electrolytic ionic water having reducing power, for example.
Further, as shown in
By lowering the processing head 60 holding the substrate so as to cover or close the top opening of the treatment tank 100 with the processing head 60 and then jetting a chemical liquid from the jet nozzles 124a of the nozzle plate 124 disposed in the treatment tank 100 toward the substrate W, the chemical liquid can be jetted uniformly onto the entire lower surface (processing surface) of the substrate W and the chemical liquid can be discharged out from the discharge pipe 126 while preventing scattering of the chemical liquid to the outside. Further, by raising the processing head 60 and closing the top opening of the treatment tank 100 with the lid 102, and then jetting a rinsing liquid from the jet nozzles 112a of the nozzle plate 112 disposed in the upper surface of the lid 102 toward the substrate W held in the processing head 60, the rinsing treatment (cleaning treatment) is carried out to remove the chemical liquid from the surface of the substrate. Because the rinsing liquid passes through the clearance between the outer tank 100a and the inner tank 100b and is discharged through the drain pipe 127, the rinsing liquid is prevented from flowing into the inner tank 100b and from being mixed with the chemical liquid.
According to the pretreatment apparatus 28, the substrate W is inserted into the processing head 60 and held therein when the processing head 60 is in the raised position, as shown in
The lowermost position of the processing head 60 may be adjusted to adjust the distance between the substrate W held in the processing head 60 and the nozzle plate 124, whereby the region of the substrate W onto which the chemical liquid is jetted from the jet nozzles 124a of the nozzle plate 124 and the jetting pressure can be adjusted as desired. Here, when the pretreatment liquid such as a chemical liquid is circulated and reused, active components are reduced by progress of the treatment, and the pretreatment liquid (chemical liquid) is taken out due to attachment of the treatment liquid to the substrate. Therefore, it is desirable to provide a pretreatment liquid management unit (not shown) for analyzing composition of the pretreatment liquid and adding insufficient components. Specifically, a chemical liquid used for cleaning is mainly composed of acid or alkali. Therefore, for example, a pH of the chemical liquid is measured, a decreased content is replenished from the difference between a preset value and the measured pH, and a decreased amount is replenished using a liquid level meter provided in the chemical storage tank. Further, with respect to a catalytic liquid, for example, in the case of acid palladium solution, the amount of acid is measured by its pH, and the amount of palladium is measured by a titration method or nephelometry, and a decreased amount can be replenished in the same manner as the above.
As shown in detail in
The suction head 234 and the substrate receiver 236 are operatively connected to each other by a splined structure such that when the substrate receiver drive cylinders 240 are actuated, the substrate receiver 236 vertically moves relative to the suction head 234, and when the substrate rotating motor 238 is energized, the output shaft 242 thereof is rotated to rotate the suction head 234 and the substrate receiver 236 in unison with each other.
As shown in detail in
The substrate receiver 236 is in the form of a downwardly open, hollow bottomed cylinder having substrate insertion windows 236a defined in a circumferential wall thereof for inserting therethrough the substrate W into the substrate receiver 236. The substrate receiver 236 also has an annular ledge 254 projecting inwardly from its lower end, and an annular protrusion 256 disposed on an upper surface of the annular ledge 254 and having a tapered inner circumferential surface 256a for guiding the substrate W.
As shown in
Further, at the top opening of the plating tank 200, there is provided a plating tank cover 270 which closes the top opening of the plating tank 200 in a non-plating time, such as idling time, so as to prevent unnecessary evaporation of the plating solution from the plating tank 200.
As shown in
Particularly, in this embodiment, by controlling the plating solution supply pump 304, the flow rate of the plating solution which is circulated at a stand by of plating or at a plating process can be set individually. Specifically, the amount of circulating plating solution at the standby of plating is in the range of 2 to 20 litter/minute, for example, and the amount of circulating plating solution at the plating process is in the range of 0 to 10 litter/minute, for example. With this arrangement, a large amount of circulating plating solution at the standby of plating can be ensured to keep a temperature of the plating bath in the cell constant, and the flow rate of the circulating plating solution is made smaller at the plating process to form a protective film (plated film) having a more uniform thickness.
The thermometer 266 provided in the vicinity of the bottom of the plating tank 200 measures a temperature of the plating solution introduced into the plating tank 200, and controls a heater 316 and a flow meter 318 described below.
Specifically, in this embodiment, there are provided a heating device 322 for heating the plating solution indirectly by a heat exchanger 320 which is provided in the plating solution in the plating solution storage tank 302 and uses water as a heating medium which has been heated by a separate heater 316 and has passed through the flow meter 318, and a stirring pump 324 for mixing the plating solution by circulating the plating solution in the plating solution storage tank 302. This is because in the plating, in some cases, the plating solution is used at a high temperature (about 80° C.), and the structure should cope with such cases. This method can prevent very delicate plating solution from being mixed with foreign matter or the like unlike an in-line heating method.
Further, on the outer surface of the peripheral wall of the cleaning tank 202 and at a position above the jet nozzles 280, there is provided a head cleaning nozzle 286 for jetting a cleaning liquid, such as pure water, inwardly and slightly downwardly onto at least a portion, which was in contact with the plating solution, of the head portion 232 of the substrate head 204.
In operating the cleaning tank 202, the substrate W held in the head portion 232 of the substrate head 204 is located at a predetermined position in the cleaning tank 202. A cleaning liquid (rinsing liquid), such as pure water, is jetted from the jet nozzles 280 to clean (rinse) the substrate W, and at the same time, a cleaning liquid such as pure water is jetted from the head cleaning nozzle 286 to clean at least a portion, which was in contact with the plating solution, of the head portion 232 of the substrate head 204, thereby preventing a deposit from accumulating on that portion which was immersed in the plating solution.
According to this electroless plating apparatus 30, when the substrate head 204 is in a raised position, the substrate W is held by vacuum attraction in the head portion 232 of the substrate head 204 as described above, while the plating solution in the plating tank 200 is allowed to circulate.
When plating is performed, the plating tank cover 270 is opened, and the substrate head 204 is lowered, while the substrate head 204 is rotating, so that the substrate W held in the head portion 232 is immersed in the plating solution in the plating tank 200.
After immersing the substrate W in the plating solution for a predetermined time, the substrate head 204 is raised to lift the substrate W from the plating solution in the plating tank 200 and, as needed, pure water (stop liquid) is immediately jetted from the jet nozzle 268 toward the substrate W to cool the substrate W, as described above. The substrate head 204 is further raised to lift the substrate W to a position above the plating tank 200, and the rotation of the substrate head 204 is stopped.
Next, while the substrate W is held by vacuum attraction in the head portion 232 of the substrate head 204, the substrate head 204 is moved to a position right above the cleaning tank 202. While rotating the substrate head 204, the substrate head 204 is lowered to a predetermined position in the cleaning tank 202. A cleaning liquid (rinsing liquid), such as pure water, is jetted from the jet nozzles 280 to clean (rinse) the substrate W, and at the same time, a cleaning liquid such as pure water is jetted from the head cleaning nozzle 286 to clean at least a portion, which was in contact with the plating solution, of the head portion 232 of the substrate head 204.
After completion of cleaning of the substrate W, the rotation of the substrate head 204 is stopped, and the substrate head 204 is raised to lift the substrate W to a position above the cleaning tank 202. Further, the substrate head 204 is moved to the transfer position between the transfer robot 16 and the substrate head 204, and the substrate W is transferred to the transfer robot 16, and is transported to a next process by the transfer robot 16.
As shown in
The plating solution management unit 330 has a dissolved oxygen densitometer 332 for measuring dissolved oxygen in the plating solution held by the electroless plating apparatus 30 by an electrochemical method, for example. According to the plating solution management unit 330, dissolved oxygen concentration in the plating solution can be controlled at a constant value on the basis of indication of the dissolved oxygen densitometer 332 by deaeration, nitrogen blowing, or other methods. In this manner, the dissolved oxygen concentration in the plating solution can be controlled at a constant value, and the plating reaction can be achieved in a good reproducibility.
When the plating solution is used repeatedly, certain components are accumulated by being carried in from the outside or decomposition of the plating solution, resulting in lowering of reproducibility of plating and deteriorating of film quality. By adding a mechanism for removing such specific components selectively, the life of the plating solution can be prolonged and the reproducibility can be improved.
The polishing power of the polishing surface of the polishing cloth 820 decreases with a continuation of a polishing operation of the CMP apparatus 32. In order to restore the polishing power, a dresser 828 is provided to conduct dressing of the polishing cloth 820, for example, at the time of replacing the substrate W. In the dressing, while rotating the dresser 828 and the polishing table 822 respectively, the dressing surface (dressing member) of the dresser 828 is pressed against the polishing cloth 820 of the polishing table 822, thereby removing the polishing liquid and chips adhering to the polishing surface and, at the same time, flattening and dressing the polishing surface, whereby the polishing surface is regenerated. The polishing table 822 may be provided with a monitor for monitoring the surface state of the substrate to detect in situ the end point of polishing, or with a monitor for inspecting in situ the finish state of the substrate.
During reversing of the substrate W, the mounting base 355 waits at a position, indicated by solid lines, below the substrate W. Before or after reversing, the mounting base 355 is raised to a position indicated by dotted lines to bring the film thickness sensors S close to the substrate W gripped by the reversing arms 353, 353, thereby measuring the film thickness.
According to this embodiment, since there is no restriction such as the arms of the transfer robot, the film thickness sensors S can be installed at arbitrary positions on the mounting base 355. Further, the mounting base 355 is adapted to be movable upward and downward, so that the distance between the substrate W and the sensors S can be adjusted at the time of measurement. It is also possible to mount plural types of sensors suitable for the purpose of detection, and change the distance between the substrate W and the sensors each time measurements are made by the respective sensors. However, the mounting base 355 moves upward and downward, thus requiring certain measuring time.
An eddy current sensor, for example, may be used as the film thickness sensors. The eddy current sensor measures a film thickness by generating an eddy current and detecting the frequency or loss of the current that has returned through the substrate W, and is used in a non-contact manner. An optical sensor may also be suitable for the film thickness sensor S. The optical sensor irradiates a light onto a sample, and measures a film thickness directly based on information of the reflected light. The optical sensor can measure a film thickness not only for a metal film but also for an insulating film such as an oxide film. Places for setting the film thickness sensor S are not limited to those shown in the drawings, but the sensor may be set at any desired places for measurement in any desired numbers.
Next, a sequence of processing for forming copper interconnects on the substrate having the seed layer 6 formed thereon which is carried out by the substrate processing apparatus having the above structure will be described with reference to
First, the substrate W having the seed layer 6 formed in its surface is taken out one by one from a transfer box 10, and is carried in the loading/unloading station 14. The substrate W which has carried in the loading/unloading station 14 is transferred to the thickness measuring instrument 24 by the transfer robot 16, and an initial film thickness (film thickness of the seed layer 6) is measured by the thickness measuring instrument 24. Thereafter, if necessary, the substrate is inverted and transferred to the plating apparatus 18. In the plating apparatus 18, as shown in
Then, the substrate W having the copper layer 7 formed thereon is transferred to the cleaning and drying apparatus 20 by the transfer robot 16, and the substrate W is cleaned by pure water and spin-dried. Alternatively, in a case where a spin-drying function is provided in the plating apparatus 18, the substrate W is spin-dried (removal of liquid) in the plating apparatus 18, and then the dried substrate is transferred to the bevel etching and backside cleaning apparatus 22.
In the bevel etching and backside cleaning apparatus 22, unnecessary copper attached to the bevel (edge) of the substrate W is removed by etching, and at the same time, the backside surface of the substrate is cleaned by pure water or the like. Thereafter, as described above, the substrate W is transferred to the cleaning and drying apparatus 20 by the transfer robot 16, and the substrate W is cleaned by pure water and spin-dried. Alternatively, in a case where a spin-drying function is provided in the bevel etching and backside cleaning apparatus 22, the substrate W is spin-dried in the bevel etching and backside cleaning apparatus 22, and then the dried substrate is transferred to the heat treatment apparatus 26 by the transfer robot 16.
In the heat treatment apparatus 26, heat treatment (annealing) of the substrate W is carried out. Then, the substrate W after the heat treatment is transferred to the film thickness measuring instrument 24 by the transfer robot 16, and the film thickness of copper is measured by the film thickness measuring instrument 24. The film thickness of the copper layer 7 (see
As shown in
In the pretreatment apparatus 28, a pretreatment before plating comprising at least one of attachment of Pd catalyst to the surface of the substrate and removal of oxide film attached to the exposed surface of the substrate, for example, is carried out. Then, the substrate after this pretreatment, as described above, is transferred to the cleaning and drying apparatus 20 by the transfer robot 16, and the substrate W is cleaned by pure water and spin-dried. Alternatively, in a case where a spin-drying function is provided in the pretreatment apparatus 28, the substrate W is spin-dried (removal of liquid) in the pretreatment apparatus 28, and then the dried substrate is transferred to the electroless plating apparatus 30 by the transfer robot 16.
In the electroless plating apparatus 30, as shown in
After the electroless plating, the substrate W is transferred to the cleaning and drying apparatus 20 by the transfer robot 16, and the surface of the substrate is cleaned by a chemical liquid, and cleaned (rinsed) with pure water, and then spin-dried by rotating the substrate at a high speed in the cleaning and drying apparatus 20. After the spin-drying, the substrate W is returned into the transfer box 10 via the loading/unloading station 14 by the transfer robot 16.
In this embodiment, copper is used as an interconnect material. However, besides copper, a copper alloy, silver, a silver alloy, and the like may be used.
As described above, according to the present invention, the plating rate in the upper part of the interconnect pattern is smaller than that in the inner part of the interconnect pattern, whereby a plated film whose surface is flat can be formed, regardless of variations of the shape of the interconnect pattern Thus, an extra plated film can be prevented from being deposited, thereby reducing low material cost, and reducing costs of a polishing process subsequent to the plating process and technical loads on the polishing process. Further, special current condition and special additives are not necessary, and the surface of the plated film is not required to be shaved, and hence the plated film of good quality can be obtained.
Number | Date | Country | Kind |
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2003-195406 | Jul 2003 | JP | national |