The present disclosure relates to a film forming method and a film forming apparatus.
Patent Document 1 discloses a method of selectively depositing a film on a top surface between trenches. In addition, Patent Document 2 discloses a method of selectively forming a film on a specific region of a substrate without using a photolithography technique. This method includes selectively forming a Si adsorption site on a flat surface of the substrate among the flat surface of the substrate and a wall surface of a trench recessed from the flat surface.
Patent Document 1: Specification of U.S. Pat. No. 10340135
Patent Document 2: Japanese Patent Laid-Open Publication No. 2018-117038
An aspect of the present disclosure provides a technique of expanding a step difference on a surface of a substrate including a recess and a protrusion which are adjacent to each other.
A film forming method of an aspect of the present disclosure includes (A) to (C) below. (A) A liquid to a surface of a substrate including a recess and a protrusion, which are adjacent to each other, is supplied on the surface. (B) A processing gas that chemically changes the liquid is supplied to the surface of the substrate to move the liquid from the recess to the protrusion by a reaction between the liquid and the processing gas and to form a film on a top surface of the protrusion, thereby expanding a step difference formed on the surface. (C) A portion of the film is etched.
According to an aspect of the present disclosure, it is possible to expand a step difference on a surface of a substrate including a recess and a protrusion which are adjacent to each other.
Hereinafter, embodiments of the present disclosure will be described with reference to the drawings. In each drawing, the same or corresponding components may be denoted by the same reference numerals, and a description thereof may be omitted.
An example of a film forming method will be described with reference to
In step S1 of
The recess Wb and the protrusion Wc are formed, for example, on the surface of the silicon wafer W1. The substrate W may include a film (not illustrated) formed on the surface of the silicon wafer W1, and the film may have a recess Wb and a protrusion Wc. The film may include one or more selected among an insulating film, a conductive film, and a semiconductor film. The recess Wb is a trench, a hole, or the like. The hole includes a via hole. The protrusion Wc may be a pillar, a fin, or the like.
The substrate surface Wa includes, for example, the bottom surface Wb1 of the recess, the side surface Wb2 of the recess, and the top surface Wc1 of the protrusion. For example, the top surface Wc1 of the protrusion is a flat surface, and the recess Wb is recessed from the top surface Wc1 of the protrusion. The depth of the recess Wb represents the size of a step difference.
The initial depth A0 of the recess Wb is, for example, 3 nm to 10,000 nm. The initial width B0 of the recess Wb is, for example, 1 nm to 1,000 nm. The ratio of the initial depth A0 to the initial width B0 (A0/B0) is, for example, 0.05 to 200.
In step S2 of
The liquid L preferably has strong intermolecular force. As the intermolecular force is increases, so does the cohesive force. When the cohesive force of the liquid L is large, evaporation of the liquid L can be prevented. The intermolecular force of the liquid L is, for example, 30 KJ/mol or more.
The liquid L is, for example, a halide. A liquid halide is formed, for example, by a reaction between a raw material gas of the halide and a reaction gas that reacts with the raw material gas. The production of the liquid L may be promoted by plasmatizing both the raw material gas and the reaction gas, or the reaction gas. The raw material gas is, for example, TiCl4 gas, and the reaction gas is, for example, H2 gas.
TiCl4 gas and H2 gas are generally used not for forming the liquid L, but for forming a Ti film. The Ti film is formed by, for example, a chemical vapor deposition (CVD) method or an atomic layer deposition (ALD) method. In the CVD method, TiCl4 gas and H2 gas are simultaneously supplied to the substrate W. On the other hand, in the ALD method, TiCl4 gas and H2 gas are alternately supplied to the substrate W. According to the CVD method or the ALD method, it is estimated that Equations (1) to (3) below contribute to the formation of a Ti film.
In the Equations (2) and (3) above, TiCl2 may be TiCl or TiCl3.
In forming a Ti film, the temperature of the substrate W is controlled to 400 degrees C. or higher. As a result, the reactions of Equations (1) to (3) above proceed in sequence, and a Ti film is formed.
On the other hand, in forming the liquid L, the temperature of the substrate W is controlled to −100 degrees C. to 390 degrees C., preferably 20 degrees C. to 350 degrees C. As a result, the reaction of Equation (2) above and the reaction of Equation (3) above are suppressed, so that a liquid L containing TiHxCly is formed. The liquid L may contain Ti, TiCl, TiCl2, TiCl3, or TiCl4. The temperature of the substrate W only need to be lower than the decomposition point of the liquid L.
The raw material gas is not limited to TiCl4 gas. For example, the raw material gas may be a halogenated silicon gas such as SiCl4 gas, Si2Cl6 gas, or SiHCl3 gas, or a metal halide gas WCl4 gas, VCl4 gas, AlCl3 gas, MoCl5 gas, SnCl4 gas, or GeCl4 gas. The raw material gas only needs to contain halogen, and the halogen may include bromine (Br), iodine (I), fluorine (F), or the like instead of chlorine (Cl). When the temperature of the substrate W is low, a reaction similar to Equation (1) above will mainly proceed with these raw material gases, so that a halide liquid L is formed.
In addition, the reaction gas is not limited to H2 gas. The reaction gas only needs to be a gas that is capable of forming the liquid L by reaction with the raw material gas. For example, the reaction gas may be D2 gas. The reaction gas may be supplied together with an inert gas such as argon gas.
Step S2 includes, for example, supplying a raw material gas and a reaction gas to the substrate W at the same time. In this case, step S2 may further include plasmatizing both the raw material gas and the reaction gas. By the plasmatization, the reaction between the raw material gas and the reaction gas can be promoted. In addition, the plasmatization makes it easier to form the liquid L at a low substrate temperature.
In addition, step S2 includes supplying the raw material gas and the reaction gas to the substrate W at the same time in the present embodiment, but may also include supplying the raw material gas and the reaction gas to the substrate W alternately. In the latter case, step S2 may further include plasmatizing the reaction gas. By the plasmatization, the reaction between the raw material gas and the reaction gas can be promoted. In addition, the plasmatization makes it easier to form the liquid L at a low substrate temperature. Furthermore, step S2 may include supplying only the raw material gas to the substrate W.
The liquid L only needs to have strong intermolecular force and may be an ionic liquid, a liquid metal, a liquid polymer, or the like. The metal may be a pure metal or an alloy. The polymer may be, for example, an oligomer or polymer formed by polymerizing two or more molecules of Si2Cl6 gas, SiCl4 gas, SiHCl3 gas, SiH2Cl2 gas, SiH3Cl gas, SiH4 gas, Si2H6 gas, Si3H8 gas, Si4H10 gas, cyclohexasilane gas, tetraethoxysilane (TEOS) gas, dimethyldiethoxysilane (DMDEOS) gas, 2,4,6,8-tetramethylcyclotetrasiloxane (TMCTS) gas, trisilylamine (TSA) gas, or the like or may be, for example, polysiloxane, polysilane, or polysilazane. In addition, the liquid L may be silanol or the like. These liquids L are supplied to the recess Wb of the substrate W by a spin coating method, or are synthesized inside a processing container that accommodates the substrate W, and is then supplied to the recess Wb of the substrate W.
In step S3 of
The film W2 may also be formed on the bottom surface Wb1 of the recess. When the thickness of the film W2 on the bottom surface Wb1 of the recess is smaller than the thickness of the film W2 on the top surface Wc1 of the protrusion, the step difference in the substrate surface Wa can be expanded.
The film W2 may also be formed on the side surface Wb2 of the recess. When the thickness of the film W2 on the side surface Wb2 of the recess is smaller than the thickness of the film W2 on the top surface Wc1 of the protrusion, the step difference on the substrate surface Wa can be expanded by forming the film W2, for example, even if the film W2 is isotropically etched.
The thickness of the film W2 on the side surface Wb2 of the recess may be zero. It is sufficient that adjacent side surfaces Wb2 of the recess are not connected to each other and the recess Wb is not closed. This is because if the recess Wb is closed, the step difference will disappear.
The film W2 may be a solid or a viscous body. The thickness of the film W2 can be controlled by the supplied amount of the liquid L.
The processing gas G is supplied, for example, from a space above the substrate surface Wa, and reacts with the liquid L. The liquid L chemically changes by reacting with the processing gas G. Since the chemical change gradually proceeds from the surface of the liquid L, a difference in surface tension occurs, and volumetric expansion or volumetric contraction occurs from the surface of the liquid L, thereby making the liquid L unstable and causing convection. Since the surface of the liquid L changes into a substance with a strong surface tension due to the reaction with the processing gas G, the liquid L moves toward the top surface Wc1 of the protrusion. In addition, the liquid L moves toward the top surface Wc1 of the protrusion by being dragged by the increase and decrease in volume due to the chemical change on the surface of the liquid L. Although not illustrated, all of the liquid L may eventually move to the top surface Wc1 of the protrusion by reaction with the processing gas G.
During the chemical change of the liquid L, degassing occurs from the liquid L due to the reaction between the liquid L and the processing gas G. The movement of the liquid L due to the occurrence of degassing is also considered to be a factor contributing to the movement of the liquid L. In addition, it is considered that minute vibrations of the substrate W may also be a factor contributing to the movement of the liquid L.
The processing gas G contains, for example, elements to be introduced into the liquid L by the reaction with the liquid L. That is, the processing gas G includes elements that are introduced into the film W2. For example, oxygen in the processing gas G is introduced into the liquid L, so that an oxide film W2 is obtained. Alternatively, nitrogen in the processing gas G is introduced into the liquid L, so that a nitride film W2 is obtained. The elements in the processing gas G only need to be introduced into the liquid L, and the elements constituting the liquid L may be degassed during the process.
For example, the processing gas G includes an oxygen-containing gas. The oxygen-containing gas contains oxygen as an element to be introduced into the liquid L. The oxygen-containing gas may further contain nitrogen as an element to be introduced into the liquid L. The oxygen-containing gas includes, for example, O2 gas, O3 gas, H2O gas, NO gas, or N2O gas.
The processing gas G may include a nitrogen-containing gas. The nitrogen-containing gas includes nitrogen as an element to be introduced into the liquid L. The nitrogen-containing gas includes, for example, N2 gas, NH3 gas, N2H4 gas, or N2H2 gas.
The processing gas G may include a hydride gas. The hydride gas contains, as the element to be introduced into the liquid L, an element bonded to hydrogen, such as Si, Ge, B, C, or P. The hydride gas includes, for example, a hydrocarbon gas such as SiH4 gas, Si2H6 gas, GeH4 gas, B2H6 gas, C2H4 gas, or PH3 gas.
The processing gas G may degas the elements constituting the liquid L by the reaction with the liquid L. For example, the processing gas G includes a reducing gas. The reducing gas is, for example, hydrogen (H2) gas or deuterium (D2) gas.
The processing gas G may be supplied together with an inert gas such as argon gas.
Step S3 may include plasmatizing the processing gas G. By the plasmatization, the reaction between the processing gas G and the liquid L can be promoted.
In step S4 in
The modifying of the film W2 includes, for example, at least one of the following (A) to (B). (A) A halogen element or hydrogen element in the film W2 is reduced. (B) The film W2 is densified. The densification of the film W2 can be achieved, for example, by terminating dangling bonds in the film W2 with an element contained in a modifying gas, or by promoting bonds between existing elements in the film W2.
In step S4, a modifying gas may be supplied to the film W2. When the modifying gas in S4 and the processing gas G in S3 are the same gas, the gases are supplied under different conditions. Specifically, for example, while the modifying gas is plasmatized, the processing gas G is not plasmatized. Alternatively, the modifying gas is supplied at a higher temperature or at a higher pressure than the processing gas G.
However, the modifying gas in S4 and the processing gas G in S3 may be different gases. For example, while the processing gas G is nitrogen gas and is plasmatized, the modifying gas is ammonia (NH3) gas and is plasmatized, or is hydrazine (N2H4) gas. Alternatively, while the process gas G is oxygen (O2) gas, the modifying gas is ozone (O3) gas or water vapor (H2O).
In step S5 of
When the number of times the first cycle has been performed is less than M times (step S5, “NO”), the size of the step difference on the substrate surface Wa is less than a target value, and thus the first cycle is performed again. M is not particularly limited, but is, for example, from 2 to 100, preferably from 5 to 20.
It is sufficient that while the first cycle is performed M times, adjacent side surfaces Wb2 of the recess are not connected to each other and the recess Wb is not closed. This is because if the recess Wb is closed, the step difference will disappear. The upper limit value of M is set so that the recess Wb is not closed.
On the other hand, when the number of times the first cycle has been performed reaches M times (step S5, “YES”), the size of the step difference on the substrate surface Wa reaches the target value, and thus the processes of step S6 and subsequent steps are performed. An example of the substrate W immediately before step S6 is illustrated in
As illustrated in
In step S6 of
Etching may be either isotropic etching or anisotropic etching. Isotropic etching and anisotropic etching may be used in combination. Isotropic etching, which is capable of etching not only the bottom surface Wb1 of the recess and the top surface Wc1 of the protrusion, but also the side surfaces Wb2 of the recess, is effective in increasing the width B of the recess Wb. On the other hand, anisotropic etching is capable of selectively etching the bottom surface Wb1 of the recess and the top surface Wc1 of the protrusion with respect to the side surfaces Wb2 of the recess.
Etching may be either dry etching or wet etching, but dry etching is preferable. In the dry etching, etching gas is supplied to the substrate surface Wa. In the dry etching, H2 gas, O2 gas, NH3 gas, or the like may be supplied to the substrate surface Wa along with the etching gas.
When dry etching is thermal etching, for example, Cl2 gas, ClF3 gas, F2 gas, HF gas, or the like is used as the etching gas. On the other hand, when the dry etching is plasma etching, for example, Cl2 gas, CF4 gas, CHF3 gas, C4F8 gas, SF6 gas, or the like is used as the etching gas to be plasmatized.
In the etching, the etching gas and the reaction gas may be supplied alternately, as in atomic layer etching (ALE). As the etching gas, for example, Cl2 gas, CF4 gas, C4F8 gas, WF6 gas, or the like is used. As the reaction gas, Ar gas, He gas, H2 gas, BCl3 gas, or the like is used. The reaction gas may be supplied after being plasmatized.
In step S7 of
When the number of times the second cycle has been performed is less than N times (step S7, “NO”), the size of the step difference on the substrate surface Wa is less than a target value, and thus the second cycle is performed again. N is not particularly limited, but is, for example, from 1 to 10, preferably from 1 to 5.
On the other hand, when the number of times the second cycle has been performed reaches N times (step S7, “YES”), the size of the step difference on the substrate surface Wa reaches the target value, and thus the processes of step S8 and subsequent steps are performed. An example of the substrate W immediately before step S8 is illustrated in
As illustrated in
In step S8 of
It is also possible to remove the protuberance on the bottom surface Wb1 of the recess by etching, as illustrated in
After etching, for example, the bottom surface Wb1 of the recess is formed by the silicon wafer, the side surface Wb2 of the recess is formed by the film W2, and the top surface Wc1 of the protrusion is formed by the film W2. When the width B of the recess Wb is returned to the initial width B0, the side surface Wb2 of the recess is formed by the film W2 and the silicon wafer.
Etching may be either isotropic etching or anisotropic etching. Isotropic etching and anisotropic etching may be used in combination. Isotropic etching, which is capable of etching not only the bottom surface Wb1 of the recess and the top surface Wc1 of the protrusion, but also the side surfaces Wb2 of the recess, is effective in increasing the width B of the recess Wb. On the other hand, anisotropic etching is capable of selectively etching the bottom surface Wb1 of the recess and the top surface Wc1 of the protrusion with respect to the side surfaces Wb2 of the recess.
Next, a film forming apparatus 1 will be described with reference to
An exhauster 24 is connected to the exhaust pipe 22 via a pressure adjuster 23. The pressure adjuster 23 includes a pressure adjustment valve such as a butterfly valve. The exhaust pipe 22 is configured such that the pressure inside the processing container 2 can be reduced by the exhauster 24. The processing container 2 is provided with a transfer port 25 on its side. The transfer port 25 is opened and closed by a gate valve 26. The loading/unloading of a wafer W between the interior of the processing container 2 and the transfer chamber (not illustrated) is performed through the transfer port 25.
A stage 3 is provided within the processing container 2. The stage 3 is a holder that holds a substrate W horizontally with the surface Wa of the substrate W facing upward. The stage 3 has a substantially circular shape in a plan view and is supported by a support member 31. A substantially circular recess 32 is formed in the surface of the stage 3 to place therein, for example, a substrate W having a diameter of 300 mm. The recess 32 has an inner diameter slightly larger than the diameter of the substrate W. The depth of the recess 32 is substantially the same as, for example, the thickness of the substrate W. The stage 3 is made of a ceramic material such as aluminum nitride (AlN). The stage 3 may be made of a metal material such as nickel (Ni). Instead of the recess 32, a guide ring configured to guide the substrate W may be provided at the peripheral edge of the surface of the stage 3.
For example, a grounded lower electrode 33 is embedded in the stage 3. A heater 34 is embedded below the lower electrode 33. The heater 34 heats the substrate W placed on the stage 3 to a set temperature by receiving power from a power supply (not illustrated) based on a control signal from the controller 100 (see
The lifting mechanism 44 is installed, for example, under the exhaust chamber 21. A bellows 45 is provided between an opening 211 for the lifting shaft 43 formed in the bottom surface of the exhaust chamber 21 and the lifting mechanism 44. The support plate 42 may have a shape that can be raised/lowered without interfering with the support member 31 of the stage 3. The lifting pins 41 are configured to be raised/lowered by the lifting mechanism 44 between the upper side of the surface of the stage 3 and the lower side of the surface of the stage 3.
A gas supplier 5 is provided on the ceiling wall 27 of the processing container 2 via an insulating member 28. The gas supplier 5 forms an upper electrode and faces the lower electrode 33. A radio-frequency power supply 512 is connected to the gas supplier 5 via a matcher 511. By supplying radio-frequency power of 450 kHz to 2.45 GHz, preferably, 450 KHz to 100 MHZ from the radio-frequency power supply 512 to the upper electrode (the gas supplier 5), a radio-frequency electric field is generated between the upper electrode (the gas supplier 5) and the lower electrode 33 and generates capacitively coupled plasma. A plasma generator 51 includes a matcher 511 and a radio-frequency power supply 512. The plasma generator 51 is not limited to capacitively coupled plasma and may generate other plasma such as inductively coupled plasma.
The gas supplier 5 includes a hollow gas supply chamber 52. In the bottom surface of the gas supply chamber 52, for example, a large number of holes 53 configured to disperse and supply a processing gas into the processing container 2 are evenly arranged. A heater 54 is embedded in the gas supplier 5, for example, above the gas supply chamber 52. The heater 54 is heated to a set temperature by being fed with power from a power supply (not illustrated) based on a control signal from the controller 100.
The gas supply chamber 52 is provided with a gas supply path 6. The gas supply path 6 communicates with the gas supply chamber 52. Gas sources G61, G62, G63, G64, and G65 are connected upstream of the gas supply path 6 via gas lines L61, L62, L63, L64, and L65, respectively.
The gas source G61 is a TiCl4 gas source, and is connected to the gas supply path 6 via the gas line L61. The gas line L61 is provided with a mass flow controller M61, a storage tank T61, and a valve V61 in that order from the gas source G61 side. The mass flow controller M61 controls the flow rate of TiCl4 gas flowing through the gas line L61. The storage tank T61 may store the TiCl4 gas supplied from the gas source G61 via the gas line L61 in the state in which the valve V61 is closed, so that the pressure of the TiCl4 gas in the storage tank T61 can be increased. The valve V61 supplies and shuts off TiCl4 gas to/from the gas supply path 6 by opening and closing operations.
The gas source G62 is an Ar gas source, and is connected to the gas supply path 6 via the gas line L62. The gas line L62 is provided with a mass flow controller M62 and a valve V62 in that order from the gas source G62 side. The mass flow controller M62 controls the flow rate of Ar gas flowing through the gas line L62. The valve V62 supplies and shuts off Ar gas to/from the gas supply path 6 by opening and closing operations.
The gas source G63 is an O2 gas source, and is connected to the gas supply path 6 via the gas line L63. The gas line L63 is provided with a mass flow controller M63 and a valve V63 in that order from the gas source G63 side. The mass flow controller M63 controls the flow rate of O2 gas flowing through the gas line L63. The valve V63 supplies and shuts off O2 gas to/from the gas supply path 6 by opening and closing operations.
The gas source G64 is a H2 gas source, and is connected to the gas supply path 6 via the gas line L64. The gas line L64 is provided with a mass flow controller M64 and a valve V64 in that order from the gas source G64 side. The mass flow controller M64 controls the flow rate of H2 gas flowing through the gas line L64. The valve V64 supplies and shuts off H2 gas to/from the gas supply path 6 by opening and closing operations.
The gas source G65 is a ClF3 gas source, and is connected to the gas supply path 6 via the gas line L65. The gas line L65 is provided with a mass flow controller M65 and a valve V65 in that order from the gas source G65 side. The mass flow controller M65 controls the flow rate of ClF3 gas flowing through the gas line L65. The valve V65 supplies and shuts off ClF3 gas to/from the gas supply path 6 by opening and closing operations.
The film forming apparatus 1 includes a controller 100 and a storage 101. The controller 100 includes a CPU, RAM, ROM, and the like (all of which are not illustrated) and controls the film forming apparatus 1 in an integrated manner by causing the CPU to execute, for example, a computer program stored in the ROM or storage 101. Specifically, the controller 100 causes the CPU to execute a control program stored in the storage 101 to control the operation of each component of the film forming apparatus 1, thereby performing a film forming process or the like on a substrate W.
Next, referring again to
Next, in step S2 of
The specific processing conditions of step S2 are, for example, as follows.
Flow rate of TiCl4 gas: 1 sccm to 100 sccm
Flow rate of Ar gas: 10 sccm to 100,000 sccm, preferably 100 sccm to 20,000 sccm
Flow rate of H2 gas: 1 sccm to 50,000 sccm, preferably 10 sccm to 10,000 sccm
Processing time: 1 second to 1,800 seconds
Processing temperature: −100 degrees C. to 390 degrees C., preferably 20 degrees C. to 350 degrees C.
Processing pressure: 0.1 Pa to 10,000 Pa, preferably 0.1 Pa to 2,000 Pa.
In step S2, the controller 100 may generate plasma by the plasma generator 51 to promote the reaction between the TiCl4 gas and the H2 gas. When supplying the TiCl4 gas and the H2 gas at the same time, the controller 100 plasmatizes both the TiCl4 gas and the H2 gas.
In step S2, the controller 100 may alternately supply the TiCl4 gas and the H2 gas into the processing container 2 instead of supplying the gases at the same time. In this case, the controller 100 may plasmatize only the H2 gas among the TiCl4 gas and the H2 gas.
After step S2, valves V61 and V64 are closed. At this time, since the valve V62 is open, Ar is supplied into the processing container 2, the gas remaining in the processing container 2 is discharged to the exhaust pipe 22, and the interior of the processing container 2 is replaced with an Ar atmosphere.
Next, in step S3 of
The specific processing conditions of step S3 are, for example, as follows.
Flow rate of O2 gas: 1 sccm to 100,000 sccm, preferably 1 sccm to 10,000 sccm
Flow rate of Ar gas: 10 sccm to 100,000 sccm, preferably 100 sccm to 20,000 sccm
Processing time: 1 second to 1,800 seconds
Processing temperature: −100 degrees C. to 390 degrees C., preferably 20 degrees C. to 350 degrees C.
Processing pressure: 0.1 Pa to 10,000 Pa, preferably 0.1 Pa to 2,000 Pa.
Next, in step S4 of
After step S4, the valve V63 is closed. At this time, since the valve V62 is open, Ar is supplied into the processing container 2, the gas remaining in the processing container 2 is discharged to the exhaust pipe 22, and the interior of the processing container 2 is replaced with an Ar atmosphere.
Next, in step S5 of
When the number of times the first cycle has been performed is less than M times (step S5, “NO”), the controller 100 performs the first cycle again. On the other hand, when the number of times the first cycle has been performed reaches M times (step S5, “YES”), the controller 100 performs step S6.
Next, in step S6 of
The specific processing conditions of step S6 are, for example, as follows.
Flow rate of ClF3 gas: 1 sccm to 100 sccm
Flow rate of Ar gas: 10 sccm to 100,000 sccm, preferably 100 sccm to 20,000 sccm
Processing time: 1 second to 1,800 seconds
Processing temperature: 30 degrees C. to 350 degrees C., preferably 80 degrees C. to 200 degrees C.
Processing pressure: 0.1 Pa to 10,000 Pa, preferably 0.1 Pa to 2,000 Pa.
After step S6, the valve V65 is closed. At this time, since the valve V62 is open, Ar is supplied into the processing container 2, the gas remaining in the processing container 2 is discharged to the exhaust pipe 22, and the interior of the processing container 2 is replaced with an Ar atmosphere.
In addition, step S6 and steps S2 to S4 are performed inside the same processing container 2 in the present embodiment, but may be performed inside different processing containers 2.
Next, in step S7 of
When the number of times the second cycle has been performed is less than N times (step S7, “NO”), the controller 100 performs the second cycle again. On the other hand, when the number of times the second cycle has been performed reaches N times (step S7, “YES”), the controller 100 performs step S8.
Next, in step S8 of
Since the specific processing conditions of step S8 are the same as those of step S6, a description thereof will be omitted. After step S8, the valve V65 is closed. At this time, since the valve V62 is open, Ar is supplied into the processing container 2, the gas remaining in the processing container 2 is discharged to the exhaust pipe 22, and the interior of the processing container 2 is replaced with an Ar atmosphere.
In addition, step S8 and steps S2 to S4 are performed inside the same processing container 2 in the present embodiment, but may be performed inside different processing containers 2.
After step S8, the controller 100 unloads the substrate W from the processing container 2 in a procedure reverse to loading the substrate W into the processing container 2.
Next, examples and the like will be described. Among Examples 1 to 23 below, Examples 1 to 19 and Example 23 are reference examples, and Examples 20 to 22 are examples of the present disclosure. In Examples 1 to 18 and 23 below, before substrates W were loaded into the processing container 2 illustrated in
In Examples 1 and 2, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
In Table 1, the “protrusion top surfaces” is the material of the protrusion top surfaces Wd formed in advance before performing step S2. The material of the side surfaces of the recesses formed in advance before performing step S2 is the same as the material of the protrusion top surfaces Wd. The “recess bottom surfaces” is the material of the bottom surfaces of the recesses formed in advance before performing step S2. In addition, “O” for various gases means that the various gases were supplied, and “ON” for “RF” means that gases was plasmatized by RF power. In addition, the “number of cycles” is the number of repetitions of steps S2 and S3 (that is, M in step S5). The same applies to Tables 2 to 8 which will be described later.
In Example 3, by using the film forming apparatus 1 shown in
In Examples 4 to 7, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
As is clear from Examples 4 to 7, it was possible to selectively form films W5 on the protrusion top surfaces Wd by using various types of processing gases G.
In Examples 8 to 12, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
As is clear from Examples 8 to 12, it was possible to selectively form films W5 on the protrusion top surfaces Wd by using substrates made of various materials.
In Examples 13 to 14, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
As is clear from Examples 13 and 14, it was possible to selectively form films W5 on the protrusion top surfaces Wd at various temperatures of substrates.
In Example 15, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
When the film W5 formed on the protrusion top surfaces Wd in Example 15 was etched with an aqueous solution having an HF concentration of 0.5% by mass, the etching rate was 762.8 Å/min. On the other hand, when the film W5 formed on the protrusion top surfaces Wd in Example 16 was etched with an aqueous solution having an HF concentration of 0.5% by mass, the etching rate was 81.3 Å/min. Therefore, it was possible to modify the film W5 by step S5.
In Example 17, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
In Example 18, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
As is clear from Examples 17 and 18, it was possible to selectively form films W5 on the protrusion top surfaces Wd by using various raw material gases.
In Example 19, four substrates W having different initial depths A0 were prepared. The initial depths A0 of the four prepared substrates W were 8 nm, 12 nm, 18 nm, and 150 nm, respectively. For the substrate W having an initial depth A0 of 8 nm, 12 nm, or 18 nm, recesses and protrusions were formed by etching silicon wafers. On the other hand, for the substrate having an initial depth A0 of 150 nm, a SiN film and a Si film were formed in that order on the surface of a silicon wafer, and recesses and protrusions were formed by etching the Si film. The SiN film was made to function as an etching stopper film that stops etching.
In Example 19, steps S1 to S5 were performed by using the film forming apparatus 1 illustrated in
In Table 9, “O” for various gases means that the various gases were supplied, and “ON” for “RF” means that gases was plasmatized by RF power. The same applies to Tables 10 to 12 and 14, which will be described later.
As shown in
On the other hand, as shown in
In Example 20, three substrates W having different initial depths A0 were prepared. The initial depths A0 of the three prepared substrates W were 8 nm, 12 nm, and 18 nm, respectively. These substrates W had recesses and protrusions formed by etching silicon wafers.
In Example 20, steps S1 to S7 were performed by using the film forming apparatus 1 illustrated in
As shown in
Furthermore, as is clear from a comparison between
In Example 21, three substrates W having different initial depths A0 were prepared. The initial depths A0 of the three prepared substrates W were 8 nm, 12 nm, and 18 nm, respectively. These substrates W had recesses and protrusions formed by etching silicon wafers.
In Example 21, steps S1 to S7 were performed by using the film forming apparatus 1 illustrated in
As shown in
Furthermore, as is clear from a comparison between
In Example 22, four substrates W having different initial depths A0 were prepared. The initial depths A0 of the four prepared substrates W were 8 nm, 12 nm, 18 nm, and 150 nm, respectively. For the substrates W having an initial depth A0 of 8 nm, 12 nm, or 18 nm, recesses and protrusions were formed by etching silicon wafers. On the other hand, for the substrate having an initial depth A0 of 150 nm, a SiN film and a Si film were formed in that order on the surface of a silicon wafer, and recesses and protrusions were formed by etching the Si film. The SiN film was made to function as an etching stopper film that stops etching.
In Example 22, steps S1 to S7 were performed by using the film forming apparatus 1 illustrated in
As shown in
Furthermore, as is clear from a comparison between
On the other hand, as shown in
Table 13 represents the sizes of step differences of the substrates obtained in Examples 19 to 22 (however, in all of Examples 19 to 22, the initial depth of the recesses Wb was 18 nm) in comparison with each other. The sizes of the step differences are represented by the depths A of the recesses Wb.
As is clear from a comparison of Examples 20 to 22 in Table 13, it can be seen that when the second cycle is repeatedly performed, it is possible to expand a step difference while securing the width B of recesses Wb. In addition, the reason why the step difference in Example 20 is smaller than that in Example 19 is that the film W2 was etched in Example 20.
In Example 23, steps S1 to S3 and S5 were performed by using the film forming apparatus 1 illustrated in
Regarding the above-described embodiment, the following appendices are disclosed.
A film forming method including:
The film forming method set forth in Appendix 1, wherein a first cycle including the process of (A) and the process of (B) is performed M times (M is an integer of 1 or more), and the process of (C) is performed after the M times of the first cycle.
The film forming method set forth in Appendix 2, wherein a second cycle including the M times of the first cycle and the process of (C) performed after the M times of the first cycle is performed N times (N is an integer of 1 or more).
The film forming method set forth in Appendix 3, further including etching the film after performing the second cycle N times to expose, on a bottom surface of the recess, a material different from the film.
The film forming method set forth in any one of Appendices 1 to 4, wherein before performing the process of (A), the step difference formed on the surface of the substrate is 20 nm or less.
The film forming method set forth in any one of Appendices 1 to 5, wherein the liquid is a halide.
The film forming method set forth in Appendix 6, wherein the process of (A) includes forming the liquid by a reaction between a raw material gas that is a raw material for the halide and a reaction gas that reacts with the raw material gas.
The film forming method set forth in any one of Appendices 1 to 5, wherein the liquid is a liquid polymer.
The film forming method set forth in Appendix 8, wherein the liquid is synthesized in a processing container that accommodates the substrate, and is supplied to the recess of the substrate.
The film forming method set forth in any one of Appendices 1 to 9, wherein the processing gas that chemically changes the liquid in the process of (B) contains an element that is introduced into the liquid.
The film forming method set forth in Appendix 10, wherein the processing gas that chemically changes the liquid includes an oxygen-containing gas.
The film forming method set forth in Appendix 10, wherein the processing gas that chemically changes the liquid includes a nitrogen-containing gas.
The film forming method set forth in Appendix 10, wherein the processing gas that chemically changes the liquid includes a hydride gas.
The film forming method according to any one of Appendices 1 to 9, wherein the processing gas that chemically changes the liquid degasses an element constituting the liquid.
The film forming method set forth in Appendix 14, wherein the processing gas that chemically changes the liquid includes a reducing gas.
The film forming method set forth in Appendix 15, wherein the reducing gas is hydrogen gas or deuterium gas.
The film forming method set forth in any one of Appendices 1 to 16, wherein the process of (B) includes plasmatizing the processing gas that chemically changes the liquid.
The film forming method set forth in any one of Appendices 1 to 17, wherein the process of (C) includes etching a portion of the film with an etching gas.
The film forming method set forth in any one of Appendices 1 to 18, further including modifying the film after the process of (B) and before the process of (C).
Number | Date | Country | Kind |
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2021-093209 | Jun 2021 | JP | national |
Filing Document | Filing Date | Country | Kind |
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PCT/JP2022/021524 | 5/26/2022 | WO |