This application is based upon and claims the benefit of priority from Japanese Patent Application No. 2021-146056, filed on Sep. 8, 2021, the entire contents of which are incorporated herein by reference.
The present disclosure relates to a film forming method, a method of manufacturing a semiconductor device, and a film forming apparatus.
Titanium silicide is used for a Si contact in a semiconductor device. Non-Patent Document 1 describes a method of sequentially depositing Ti and TiN on a Si substrate and then reacting Ti with Si of the substrate by annealing to form titanium silicide (TiSi2). Patent Document 1 describes forming a TiSi2 layer on a silicon substrate by an atomic layer deposition (ALD) method using TiCl4 and SiH4. In addition, Non-Patent Document 2 describes forming a TiSi2 film by a chemical vapor deposition (CVD) method using TiI4 and SiH4.
According to one embodiment of the present disclosure, there is provided a film forming method of forming a titanium silicide film in a contact forming region of a substrate. The film forming method includes: preparing the substrate having the contact forming region; and forming the titanium silicide film in the contact forming region of the substrate by atomic layer deposition (ALD) by sequentially supplying TiI4 gas as a Ti precursor and a Si-containing gas as a reducing gas to the substrate.
The accompanying drawings, which are incorporated in and constitute a part of the specification, illustrate embodiments of the present disclosure, and together with the general description given above and the detailed description of the embodiments given below, serve to explain the principles of the present disclosure.
Reference will now be made in detail to various embodiments, examples of which are illustrated in the accompanying drawings. In the following detailed description, numerous specific details are set forth in order to provide a thorough understanding of the present disclosure. However, it will be apparent to one of ordinary skill in the art that the present disclosure may be practiced without these specific details. In other instances, well-known methods, procedures, systems, and components have not been described in detail so as not to unnecessarily obscure aspects of the various embodiments.
Hereinafter, embodiments will be described with reference to the accompanying drawings.
First, the background and outline of a film forming method according to the present disclosure will be described.
Since TiSi2 and TiSi are present in titanium silicide, titanium silicide will be referred to as TiSix including both TiSi2 and TiSi in the following description.
When forming a TiSix film used for Si contacts, from the viewpoint of reducing the risk of device failure due to thermal budget, it is required to lower a processing temperature. Especially, 450 degrees C. or less is required for a logic semiconductor having a low heat resistance. Further, along with miniaturization of semiconductor devices, especially in a logic semiconductor, the TiSix film used for a Si contact is required to have a low resistance.
A Si contact is formed in an impurity diffusion region such as a source electrode or a drain electrode. However, when Ti is reacted with Si of a substrate (reduction reaction) by annealing to form a TiSix film as in Non-Patent Document 1, impurities added to Si due to the reaction between Ti and Si (reduction reaction) are also sucked up at the same time. Since a contact resistance is proportional to a resistance and Schottky barrier of a material and inversely proportional to an impurity concentration at a metal (Ti)—Si interface, when the impurities are sucked up from the impurity diffusion region and the impurity concentration is decreased, the contact resistance increases. Further, in Non-Patent Document 1, the processing temperature required for the reaction for forming TiSix is as high as 650 degrees C. or higher. Therefore, it is difficult to apply the technique of Non-Patent Document 1 to a logic semiconductor.
In addition, in Patent Document 1, a TiSix layer is epitaxially grown on a silicon substrate by ALD using TiCl4 and SiH4. However, a high film forming temperature is required. In addition, Non-Patent Document 2 describes that a TiSi2 film is formed by CVD using TiI4 and SiH4. However, a substrate temperature at that time is as high as 650 degrees C.
Therefore, studies have been made to implement the recent demands for lowering the processing temperature and lowering the resistance of a TiSix film constituting a Si contact. As a result, it was found that it is effective to directly form a TiSix film on a contact forming region of a substrate by ALD using TiI4 gas and a Si-containing gas.
Next, a film forming method according to an embodiment of the present disclosure will be described.
The substrate prepared in step ST1 is configured as shown in
In step ST2, the TiI4 gas, which is a Ti precursor, and the Si-containing gas, which is a reducing gas (siliciding gas), are sequentially (typically, alternately) supplied to the substrate 101 in a processing container. Thus, as shown in
After forming the TiSix film 105, as shown in
Prior to the film forming process of step ST2, a process of removing a natural oxide film formed on the surface of the contact forming region 104 may be performed. The natural oxide film can be removed by a precleaning process using Ar sputtering or the like.
In addition, after step ST2, a plasma process may be performed by H2 plasma or the like.
Next, the film forming process of step ST2 will be described in detail.
In the formation of the TiSix film 105 in step ST2, TiI4 used as a Ti precursor has high reactivity. Therefore, the reaction with a Si compound gas can occur at a low temperature, and the TiSix film can be formed at the low temperature.
TiI4(g)+2SiH4(g)=TiSi2+2I2(g)+4H2(g) (1)
TiBr4(g)+2SiH4(g)=TiSi2+2Br2(g)+4H2(g) (2)
TiCl4(g)+2SiH4(g)=TiSi2+2Cl2(g)+4H2(g) (3)
As shown in the simulation result of
When the TiSix film is formed by ALD using the TiI4 gas and the Si-containing gas as described above, film formation can be performed at the low temperature of 450 degrees C. or lower. Therefore, even in the case of a logic semiconductor, it is possible to reduce the risk of device defects due to thermal budget. Further, instead of forming silicide by a reaction with the underlying Si, the TiSix film is directly formed on the contact forming region 104 by ALD. Therefore, it is possible to prevent impurities such as B and the like from being sucked up from the contact forming region 104. This makes it possible to reduce the resistance of the Si contact.
In addition, since an ALD method has high film thickness controllability, the TiSix film can be made thin by forming the TiSix film by ALD. A film thickness of the TiSix film may be in a range of 0.5 nm to 10 nm.
Examples of the Si-containing gas used as the reducing gas include a silane-based gas, an iodide-based gas, a chloride-based gas, a bromide-based gas, and a fluoride-based gas, which are listed below.
Silane-based gas: Si2H6 and SiH4
Iodide-based gas: Si2I6, SiI4, SiHI3, SiH2I2, and SiH3I
Chloride-based gas: Si2Cl6, SiCl4, SiHCl3, SiH2Cl2, and SiH3Cl
Bromide-based gas: Si2Br6, SiBr4, SiHBr3, SiH2Br2, and SiH3Br
Fluoride-based gas: Si2F6, SiF4, SiHF3, SiH2F2, and SiH3F
Among these gases, the SiH4 gas is desirable from the viewpoint of reactivity. Further, since the iodide-based gas is the same type of gas as TiI4, it has an advantage that impurities can be reduced.
In addition to the Si-containing gas, other reducing gases may be used. As other reducing gases, it may be possible to use H2 gas, a deuterium-containing gas, and NH3 gas. The deuterium-containing gas means a deuterium gas that is a gas of deuterium molecules in each which two deuterium atoms are bonded, or a gas of molecules in each which one protium atom and one deuterium atom are bonded. By using at least one of the H2 gas, the deuterium-containing gas, and the NH3 gas as other reducing gases in addition to the Si-containing gas, it is possible to allow the reduction reaction to proceed with ease. A supply timing of other reducing gases is not particularly limited. For example, other reducing gases may be supplied each time when the Si-containing gas is supplied, or may be supplied at a part of a timing of supplying the Si-containing gas, for example, once every several times. Of course, other reducing gases may be supplied at a timing different from the supply timing of the SiH4 gas.
In step ST2, after supplying the TiI4 gas and after supplying the Si-containing gas, a residual gas in the processing container is discharged by a purge gas. As the purge gas, an inert gas may be used. As the inert gas, N2 gas or Ar gas may be desirably used. The purge gas may be continuously supplied during the film forming process.
A pressure in the processing container during step ST2 may be in a range of 13 Pa to 6,650 Pa (0.1 Torr to 50 Torr).
In step ST11, as in step ST1, the substrate 101 shown in
As shown in
As the film formation inhibitor 107, an organic substance that is easily adsorbed on the insulating film 102 is desirable. An alkyl halide or an alkene may be desirably used as the film formation inhibitor 107. An alkyl halide and an alkene are particularly easily adsorbed to a nitrogen-containing substance such as SiN or the like. The alkyl halide is represented by a general formula R—X (where R is an alkyl group and X is a halogen atom), and the alkene is a hydrocarbon (ethylene, propylene, isobutylene, or the like) having a carbon double bond.
The process of forming the film formation inhibitor in step ST12 may be performed prior to the process of forming the TiSix film in step ST13 as shown in
Next, an example of a film forming apparatus capable of carrying out the film forming method as described above will be described.
A film forming apparatus 100 includes a chamber 1 as a processing container, a susceptor (stage) 2, a shower head 3, an exhauster 4, a gas supply mechanism 5, and a controller 6.
The chamber 1, which is a processing container, includes a substantially cylindrical metal. A loading/unloading port 26 for loading and unloading a substrate W by a transfer mechanism (not shown) with respect to a vacuum transfer chamber (not shown) is formed on a side wall of the chamber 1. The loading/unloading port 26 can be opened and closed by a gate valve G.
An annular exhaust duct 28 having a rectangular cross section is provided on a main body of the chamber 1. A slit 28a is formed in the exhaust duct 28 along an inner peripheral surface thereof. In addition, an exhaust port 28b is formed on an outer wall of the exhaust duct 28. A top wall 29 is provided on an upper surface of the exhaust duct 28 so as to close an upper opening of the chamber 1. A space between the top wall 29 and the exhaust duct 28 is airtightly sealed by a seal ring 30.
The susceptor 2 as a stage is used for placing the substrate W thereon in the chamber 1. As the substrate W, a semiconductor wafer (silicon wafer) having the structure shown in
The support 33 that supports the susceptor 2 extends from a center of a bottom surface of the susceptor 2 to below the chamber 1 via a hole formed in a bottom wall of the chamber 1. A lower end of the support 33 is connected to an elevating mechanism 34. The susceptor 2 can be moved up and down by the elevating mechanism 34 via the support 33 between a processing position shown in
In a vicinity of the bottom surface of the chamber 1, three wafer support pins 37 (only two of which are shown) are provided so as to protrude upward from a lift plate 37a. The wafer support pins 37 can be raised and lowered via the lift plate 37a by a lift mechanism 38 provided below the chamber 1. The wafer support pins 37 are inserted into through-holes 22 provided in the susceptor 2 located at the transfer position so that they can protrude and retract with respect to the upper surface of the susceptor 2. As a result, the substrate W is delivered between a wafer transfer mechanism (not shown) and the susceptor 2.
A heater (not shown) is embedded inside the wall of the chamber 1, and is configured to control a temperature of an inner wall of the chamber 1 to substantially 100 degrees C. to 350 degrees C. to prevent the TiSix film from adhering to the inner wall of the chamber 1.
The shower head 3 is used for supplying a processing gas into the chamber 1 in a shower shape, and is provided at an upper portion of the chamber 1 so as to face the susceptor 2. The shower head 3 has substantially the same diameter as the susceptor 2. The shower head 3 includes a main body 39 fixed to the top wall 29 of the chamber 1 and a shower plate 40 connected to the main body 39 from below. A gas diffusion space 41 is formed between the main body 39 and the shower plate 40.
A plurality of gas dispersion members 42 is provided in the gas diffusion space 41. A plurality of gas discharge holes is formed around the gas dispersion members 42. The gas dispersion members 42 are connected to one ends of a plurality of gas supply paths 43 provided in the main body 39, respectively. The other ends of the gas supply paths 43 are connected to a diffusion portion 44 formed at a center of an upper surface of the main body 39. In addition, two gas introduction holes 45a and 45b penetrating from the upper surface of the main body 39 to the diffusion portion 44 are provided at a central portion of the main body 39.
An annular protrusion 40b protruding downward is formed on a peripheral edge of the shower plate 40. Gas discharge holes 40a are formed on a flat surface of the shower plate 40 inward of the annular protrusion 40b. When the susceptor 2 is located at the processing position, a processing space S is formed between the shower plate 40 and the susceptor 2, and the annular protrusion 40b and the upper surface of the cover 32 of the susceptor 2 are close to each other to form an annular gap 48.
The exhauster 4 includes an exhaust pipe 46 connected to the exhaust port 28b of the exhaust duct 28, and an exhaust mechanism 47 connected to the exhaust pipe 46 and provided with a vacuum pump, a pressure control valve, and the like. During the processing, the gas in the chamber 1 reaches the exhaust duct 28 via the slit 28a, and is exhausted from the exhaust duct 28 via the exhaust pipe 46 by the exhaust mechanism 47 of the exhauster 4.
The processing gas supply mechanism 5 includes a TiI4 gas source 51 for supplying TiI4 gas as a Ti precursor, and a SiH4 gas source 52 for supplying SiH4 gas as a reducing gas (siliciding gas). The processing gas supply mechanism 5 further includes a first N2 gas source 53 and a second N2 gas source 54 for supplying N2 gas as a purge gas, an R gas source 55 for supplying other reducing gases (also referred to as R gas) such as H2 gas, a deuterium-containing gas, and NH3 gas, and a film formation inhibitor source 56 for supplying a film formation inhibitor.
A TiI4 gas supply line 61 extends from the TiI4 gas source 51, and a SiH4 gas supply line 62 extends from the SiH4 gas source 52. The other ends of the TiI4 gas supply line 61 and the SiH4 gas supply line 62 are connected to the gas introduction holes 45a and 45b, respectively.
A first N2 gas supply line 63 that supplies N2 gas toward the TiI4 gas supply line 61 is connected to the first N2 gas source 53. In addition, a second N2 gas supply line 66 that supplies N2 gas toward the SiH4 gas supply line 62 is connected to the second N2 gas source 54.
The first N2 gas supply line 63 is branched into a first continuous N2 gas supply line 64 that constantly supplies N2 gas during the ALD film formation, and a first flash purge line 65 that supplies N2 gas only during a purge process. In addition, the second N2 gas supply line 66 is branched into a second continuous N2 gas supply line 67 that constantly supplies N2 gas during the ALD film formation, and a second flash purge line 68 that supplies N2 gas only during the purge process. The other end of the first continuous N2 gas supply line 64 is connected to the TiI4 gas supply line 61, and the other end of the first flash purge line 65 is connected to the first continuous N2 gas supply line 64. The other end of the second continuous N2 gas supply line 67 is connected to the SiH4 gas supply line 62, and the other end of the second flash purge line 68 is connected to the second continuous N2 gas supply line 67. Since the first flash purge line 65 and the second flash purge line 68 have large flow rate capacities, orifices 83 and 84 for preventing backflow are provided in the first continuous N2 gas supply line 64 and the second continuous N2 gas supply line 67, respectively.
An R gas supply line 69 extends from the R gas source 55, and a film formation inhibitor supply line 70 extends from the film formation inhibitor source 56. The other end of the R gas supply line 69 is connected to the second continuous N2 gas supply line 67, and the other end of the film formation inhibitor supply line 70 is connected to the R gas supply line 69.
A valve V1, a buffer tank 81, and a flow meter 71 are installed in the TiI4 gas supply line 61 sequentially from a downstream side. Further, a valve V2, a buffer tank 82, and a flow rate controller 72 are installed in the SiH4 gas supply line 62 sequentially from the downstream side. The buffer tanks 81 and 82 are used for temporarily storing the respective gases. By storing the gases, increasing internal pressures of the buffer tanks 81 and 82, and then supplying the stored gases, the buffer tanks 81 and 82 can supply the gases into the chamber 1 at a large flow rate. Buffer tanks may be provided on the first and second flash purge lines 65 and 68 that supply N2 gas at a large flow rate.
In the first continuous N2 gas supply line 64, the first flash purge line 65, the second continuous N2 gas supply line 67, and the second flash purge line 68, valves V3, V4, V5, and V6 are installed on a downstream side, and flow rate controllers 73, 74, 75 and 76 are installed on an upstream side, respectively. Flow rate controllers 77 and 78 are installed in the R gas supply line 69 and the film formation inhibitor supply line 70, respectively. In addition, a valve V7 is installed in the R gas supply line 69 on a downstream side of a merging point of the film formation inhibitor supply line 70.
The valves V1 to V7 function as ALD valves for switching gases during the ALD process, and are composed of high-speed valves that can be opened and closed at a high speed.
Although not shown, the gas supply mechanism 5 further includes a ClF3 gas supply line that supplies ClF3 gas as a cleaning gas for cleaning an interior of the chamber 1. The gas supply mechanism 5 further includes a bottom N2 gas supply line that supplies N2 gas from the bottom of the chamber 1.
Since TiI4 is in a solid state at room temperature, as shown in
A carrier gas pipe 91 for supplying N2 gas as a carrier gas, is inserted into the solid raw material tank 90 from above. A carrier N2 gas source 92 is connected to the carrier gas pipe 91. A flow rate controller 91a is installed in the carrier gas pipe 91. In addition, the above-mentioned TiI4 gas supply line 61 is inserted into the solid raw material tank 90 from above. The TiI4 gas supply line 61 is provided with a heater (not shown) for preventing condensation of the TiI4 gas. The TiI4 gas sublimated in the solid raw material tank 90 is transferred by the carrier N2 gas and supplied to the TiI4 gas supply line 61. An offset N2 gas supply line 93 is connected to the TiI4 gas supply line 61 at a portion on an upstream side of the flow meter 71, and an N2 gas source 94 is connected to the offset N2 gas supply line 93. The offset N2 gas supply line 93 is provided with a flow rate controller 93a and a valve 93b. A flow rate of the TiI4 gas is adjusted by the flow rate controller 91a of the carrier gas pipe 91 and the flow rate controller 93a of the offset N2 gas supply line 93.
The carrier gas pipe 91 and the TiI4 gas supply line 61 are connected by a bypass pipe 97. A valve 97a is installed in the bypass pipe 97. A valve 95a and a valve 95b are installed in the carrier gas pipe 91 on an upstream side and a downstream side of the connection point of the bypass pipe 97, respectively. In addition, a valve 96a and a valve 96b are installed in the TiI4 gas supply line 61 on an upstream side and a downstream side of the connection point of the bypass pipe 97, respectively. Thus, by closing the valves 95b and 96a and opening the valves 95a, 96b, and 97a, the N2 gas from the carrier N2 gas source 93 can be supplied via the carrier gas pipe 91 and the bypass pipe 97 to purge the TiI4 gas supply line 61. The TiI4 gas supply line 61 can also be purged by the N2 gas supplied from the offset N2 gas supply line 93.
At the time of purging the interior of the chamber 1, a flash purge N2 gas can be supplied from the first flash purge line 65 and the second flash purge line 68 to strengthen the purging. However, it is not essential to provide the first and second flash purge lines 65 and 68. Likewise, the buffer tanks 81 and 82 are not essential.
The controller 6 is composed of a computer, and includes a main controller equipped with a CPU, an input device (keyboard, mouse, etc.), an output device (printer, etc.), a display device (display, etc.), and a memory device (non-transitory computer-readable storage medium). The main controller controls operations of respective components, for example, opening and closing the valves V1 to V7, adjusting the gas flow rates by the flow rate controllers 72 to 78, regulating the pressure in the chamber 1 by the pressure control valve, adjusting the temperature of the substrate W by the heater 31, and the like. The control of these operations is executed by a process recipe which is a control program stored in the storage medium (hard disk, optical desk, semiconductor memory, etc.) built in the memory device.
In the film forming apparatus 100 configured as described above, under the control of the controller 6, the heater 31 heats the substrate W so that the temperature of the substrate W placed on the susceptor 2 is set to be 450 degrees C. or lower, for example, 350 degrees C.
In such a state, first, the gate valve G is opened. The substrate W is loaded into the chamber 1 from a vacuum transfer chamber (not shown) by a transfer device (not shown), and is placed on the susceptor 2. When necessary, prior to the transfer of the substrate W to the chamber 1, a natural oxide film may be removed from the substrate W by performing a precleaning process or the like in a separate chamber.
After placing the substrate W and retreating the transfer device, the gate valve G is closed and the susceptor 2 is raised to the processing position. Subsequently, the interior of the chamber 1 is exhausted by the exhauster 4, and the valves V3 and V5 are opened to continuously supply N2 gas into the processing space S of the chamber 1 via the first continuous N2 gas supply line 64 and the second continuous N2 gas supply line 67. As a result, the interior of the chamber 1 is maintained at a reduced pressure of 13 Pa to 6,650 Pa (0.1 Torr to 50 Torr), and the temperature of the substrate W on the susceptor 2 is stabilized at a desired temperature of 450 degrees C. or lower, for example, 350 degrees C.
Thereafter, while maintaining the state of continuously supplying the N2 gas, the valves V1 and V2 of the TiI4 gas supply line 61 and the SiH4 gas supply line 62 are operated to supply the TiI4 gas and the SiH4 gas alternately and intermittently. Thus, a TiSix film is formed in the contact forming region of the substrate W by ALD.
During the process, the valves V3 and V5 are kept open to continuously supply N2 gas via the first continuous N2 gas supply line 64 and the second continuous N2 gas supply line 67. Then, the valve V1 is first opened to supply TiI4 gas to the processing space S in the chamber 1 via the TiI4 gas supply line 61 (operation Si). As a result, the TiI4 gas is adsorbed on the surface of the substrate W. At this time, the TiI4 gas is temporarily stored in the buffer tank 81, subjected to a pressure increase, and then supplied into the chamber 1.
Subsequently, the valve V1 is closed to stop the supply of the TiI4 gas, and the interior of the processing space S of the chamber 1 is purged (operation S2). In the purge process performed at this time, the valves V4 and V6 are opened to supply N2 gas (flash purge N2 gas) from the first flash purge line 65 and the second flash purge line 68, in addition to the continuously supplied N2 gas. As a result, the excessive TiI4 gas or the like in the processing space S can be quickly discharged by the N2 gas supplied at a large flow rate.
Subsequently, the valves V4 and V6 are closed to stop the supply of the flash purge N2 gas, and the valve V2 is opened to supply SiH4 gas to the processing space S in the chamber 1 via the SiH4 gas supply line 62 (operation S3). As a result, the adsorbed TiI4 gas and the SiH4 gas react with each other. At this time, the SiH4 gas is temporarily stored in the buffer tank 82, subjected to a pressure increase, and then supplied into the chamber 1.
Subsequently, the valve V2 is closed to stop the supply of the SiH4 gas, and the interior of the processing space S of the chamber 1 is purged (operation S4). In the purge process performed at this time, the valves V4 and V6 are opened to supply N2 gas (flash purge N2 gas) from the first flash purge line 65 and the second flash purge line 68, in addition to the continuously supplied N2 gas. As a result, the excessive SiH4 gas or the like in the processing space S can be quickly discharged by the N2 gas supplied at a large flow rate.
By performing one cycle of the above operations S1 to S4 in a short time, a thin TiSix unit film is formed, and by repeating the cycle of the steps described above a predetermined number of times, a TiSix film having a desired film thickness is formed. The film thickness of the TiSix film formed at this time can be controlled by the repetition number of the cycle.
By using other reducing gases such as H2 gas, a deuterium-containing gas, and NH3 gas supplied from the R gas source 55 in addition to the SiH4 gas, it is possible to allow the reduction reaction to proceed with ease. The supply timing of other reducing gases is not particularly limited. For example, other reducing gases may be supplied each time when the Si-containing gas is supplied, or may be supplied at a part of the timing of supplying the Si-containing gas, for example, once every several times. In addition, other reducing gases may be supplied at the supply timing of the TiI4 gas, or may be supplied at a timing different from the supply timing of the SiH4 gas or the TiI4 gas.
The film formation inhibitor from the film formation inhibitor source 56 may be supplied as needed. By supplying the film formation inhibitor, as described above, the film formation inhibitor can be adsorbed to the region where the TiSix film is desired not to be formed, thereby suppressing formation of the TiSix film in that region. The film formation inhibitor can be supplied after the substrate W is placed on the susceptor 2 and before the TiSix film is formed by ALD. In addition, the film formation inhibitor may be supplied when the TiSix film is formed by ALD. For example, the film formation inhibitor may be sequentially supplied after the operation S2 or after the operation S4, or may be supplied when supplying the TiI4 gas in the operation Si or when supplying the SiH4 gas in the operation S3. The film formation inhibitor may be supplied both when supplying the TiI4 gas and when supplying the SiH4 gas.
After the processing of one substrate W is completed, the interior of the chamber 1 is purged with N2 gas, and the susceptor 2 is lowered to the transfer position. Subsequently, the gate valve G is opened, the transfer device is inserted into the chamber 1 from the vacuum transfer chamber, and the substrate W on the susceptor 2 is unloaded from the chamber 1.
The substrate W on which the TiSix film is formed may be transferred to another chamber and subjected to a plasma process using H2 plasma or the like.
In the film forming apparatus 100, after the film forming process on a certain number of substrates W is completed, ClF3 gas may be supplied as a cleaning gas from the ClF3 gas supply line to clean the interior of the chamber 1. The cleaning process is performed by supplying the ClF3 gas into the chamber 1 in a state in which the substrate W does not exist in the chamber 1. The inner wall of the chamber 1 is heated to substantially 100 degrees C. to 350 degrees C., and adhesion of a TiSix film is suppressed. However, the adhesion of the TiSix film cannot be completely eliminated. Therefore, the TiSix film adhering to the inner wall of the chamber 1 is removed by the ClF3 gas.
In the formation of the TiSix film by ALD in the film forming apparatus 100 as described above, the TiI4 gas having good reactivity is adsorbed on the substrate W at substantially one molecular layer with good controllability, and then the TiI4 gas is reacted with the SiH4 gas to form an extremely thin TiSix unit film. This operation is repeated a plurality of times. Therefore, it is possible to form the TiSix film at a low temperature of 450 degrees C. or lower. In addition, due to the high controllability, it is possible to form a thin TiSix film of 0.5 nm to 10 nm. In addition, since the TiSix film is directly formed in the contact forming region by ALD, it is possible to suppress impurities from being suctioned from the contact forming region and to reduce a resistance of the Si contact.
In addition, since the N2 gas (flash purge N2 gas) is supplied from the first flash purge line 65 and the second flash purge line 68 in addition to the continuously supplied N2 gas supplied in the purge process of the operations S2 and S4, the gas replaceability is high. Therefore, the purge process can be performed in a short period of time, and the controllability of the film thickness can be improved. In addition, the buffer tanks 81 and 82 are provided in the TiI4 gas supply line 61 and the SiH4 gas supply line 62, respectively, so that the TiI4 gas and the SiH4 gas can be temporarily stored therein and then discharged. Therefore, the TiI4 gas and the SiH4 gas can be easily supplied in a short time. Even when one cycle is short, it is possible to reliably supply a required amount of the TiI4 gas and the SiH4 gas.
Although the embodiments of the present disclosure have been described above, the embodiments disclosed herein should be considered to be exemplary and not limitative in all respects. The above-described embodiments may be omitted, replaced, or modified in various forms without departing from the scope of the appended claims and their gist.
For example, in the above-described embodiments, the case where the TiSix film is formed in the contact forming region of the logic semiconductor has been mainly described. However, the present disclosure may be applied to a contact forming region of a memory semiconductor such as a DRAM or a 3D NAND.
In addition, the film forming apparatus shown in
In addition, in the above-described embodiments, the semiconductor wafer has been described as an example of the substrate. However, the substrate is not limited to the semiconductor wafer and may be any substrate having a contact forming region in which a Si contact is formed. For example, the substrate may be a glass substrate used for a flat panel display (FPD) or other substrates such as a ceramic substrate and the like.
According to the present disclosure in some embodiments, it is possible to form a low-resistance titanium silicide film at a low temperature.
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 disclosures. Indeed, the 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 disclosures. The accompanying claims and their equivalents are intended to cover such forms or modifications as would fall within the scope and spirit of the disclosures.
Number | Date | Country | Kind |
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2021-146056 | Sep 2021 | JP | national |